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V. 



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*i^*Will he mailed, prepaid, on the receipt of the price. 



TABLES 



OF THE PROPERTIES OF 



SATURATED STEAM 



AND OTHER VAPORS. 



BY 



CECIL H. PEABODY, B.S., 

ASSISTANT PROFESSOR OF STEAM ENGINEERING IN THE MASSACHUSETTS INSTITUTE 

OF TECHNOLOGY. 



4^' 






NEW YORK : 
JOHN WILEY AND SONS, 

1888. 



^^IJ]^ 



"^- c 



Copyright, 1888, 
By CECIL H. PEABODY. 



(^^ 



•^^Y 



RAND AVERY COMPANY, 
ELECTROTYPERS AND PRINTERS, 



^'^ 




SATUEATBD . STEAM, AND OTHER VAPORS. 



A COMPARISON of the several tables of the properties of saturated steam, 
expressed in English units, reveals discrepancies of considerable magnitude ; 
and investigation shows that, while all are in some manner founded on the 
experiments of Regnault, various methods of calculation have been used, and 
in some cases other experimental data have been employed. A review of 
the whole subject, in connection with the preparation of notes on thermo- 
d3mamics for the use of the students of the Massachusetts Institute of 
Technology, made it seem important to calculate a set of tables, to accompany 
those notes, founded on the best and most recent data. 

In presenting the tables for general use, it appears proper to state in full 
the data and the methods of calculation employed, so that each one may 
see the degree of accuracy and correctness of the tables, and the reliance 
to be placed on them. 

Tables of the properties of other vapors have been added, which will be 
discussed hereafter. 

Pressure of Saturated Steam. — As a conclusion from all the experiments 
on the tension of saturated steam, Regnault gives, in the Memoires de 
VInstitut de France^ etc., Tome XXL, the following data : — 



TEMPERATUBE 


PRESSURE 


C. 


MM. OF MERCURY. 


-32 


0.32 


-16 


1.29 





4.60 


25 


23.55 


50 


91.98 


75 


288.50 


100 


760.00 


130 


2030.0 


160 


4651.6 


190 


9426. 


220 


17390. 


-20 


0.91 


+40 


54.91 



6 SATURATED STEAM, AND OTHER VAPORS. 

From these data he calculated, by the aid of seven-place logarithms, the 
following formulae, which give the pressure in millimetres of mercury for 
any temperature in degrees Centigrade : — 

A. For steam from —32° to 0"* C. 

p — a -\- ba". 

a = — 0.08038. 
log b = 9.6024724 - 10. 
log a = 0.033398. 

n = 32° - t. 

B. For steam from 0° to 100° C. 
log p z= a — boP- -\- cj3^. 

a = 4.7384380. 
log b = 0.6116485. 
log c = 8.1340339 - 10. 
log a = 9.9967449 - 10. 
log/?= 0.006865036. 

n = t. 

C. For steam from 100° to 220° C. 
log p = a — 6a" + c/3". 

a = 5.4583895. 
log b = 0.4121470. 
log c = 7.7448901 - 10. 
log a = 9.997412127 - 10. 
log^ = 0.007590697. 

n = t- 100. 

D. For steam from - 20° to 220° C. 
logp = a — ba"* — c^, 

a = 6.2640348. 
log b = 0.1397743. 
log c = 0.6924351. 
log a = 9.994049292 - 10. 
log^= 9.998343862 - 10. 
n = f + 20. 
B}' aid of the formulae A and jB, Regnault calculated and recorded tables 
of the pressures of saturated steam for temperatures from — 32° to 100° C. 
The formula D was calculated from the data given above for the temperatures 
- 20°, -h 40°, 100°, 160°. and 220° C, and was intended to represent the 
whole range of experiments. By this formula, instead of formula (7, he 
calculated the pressures set down in his tables for temperatures from 100° C. 
to 220° C. 

Wishuig to obtain oreater accuracy for meteorological work, Moritz re- 
calculated liquation B, using ten-place logarithms, and obtained constants 



SATURATED STEAM, AND OTHER VAPORS. 



that differ but little from those that will be given later. Some of the more 
recent tables in the French system Avere calculated by his equations. 

Equations for the Pressure of Steam at Paris. — In view of the preceding 
statements, it appeared desirable to re-calculate the constants for Equations 
B and (7, with a degree of accuracy that should exclude any doubt as to the 
reliability of the results. Accordingly, the logarithms required were taken 
from Vega's ten-place table, and then the remainder of the calculations were 
carried on with natural numbers, checkiug by independent methods, with the 
following results : — 

B. For steam from 0° to 100° C. 
log p = a — 6a" + c(^. 

a = 4.7393622142. 
logs = 0.6117400190. 
log c = 8.1320378383 - 10. 
log a = 9.996725532820 - 10. 
logi8 = 0.006864675924. 

n = t. 

C. For steam from 100° to 220° C. 
logp = a — 6a" + c^. 

a = 5.4574301234. 
log b = 0.4119787931. 



log c 



7.7417476470 - 10. 



log a = 9.99741106346 - 
log/3 = 0.007642489113. 
n = t — 100. 



10. 



To show the 



t 





25 

50 

75 

100 



t. 

100 
130 
160 
190 
220 



legree of 


accuracy attained. 
Equation B. 


the following tables 


P- 


LOG p FEOM TABLE 


LOG p CALCULATED 


OF LOGARITHMS. 


BY EQUATION. 


4.60 


0.6627578317 




23.55 


1.3719909115 


1.37199097 


91.98 


1.9636934052 


1.96369346 


288.50 


2.4601458175 


2.46014587 


760 


2.8808135923 
Equation C. 


2.88081365 


P- 


LOG p FEOM TABLE 


LOG 2? CALCULATED 


OF LOGARITHMS. 


BY EQUATION. 


760.00 


2.8808135923 




2030.0 


3.3074960379 


3.307496036 


4651.6 


3.6676023618 


3.667602359 


9426 


3.9743274354 


3.974327428 


17390 


4.2402995820 


4.240299575 



are 



8 SATUBATED STEAM, AND OTHER VAPORS. 

The results from Equation C are quite satisfactory ; for the errors come in 
the ninth place of decimals, and one place of decimals is unavoidabl}' lost 
in the application of the formula. Equation B was calculated after Equation 
C and the numerical work was not carried to so large a number of decimal 
places. For the calculation of tables, the constants are carried to seven places 
of significant figures only ; this gives six significant figures in the result, of 
which five are recorded in the table. 

Pressure of Steam at Latitude 45°. — French System. — It is customary to 
reduce all measurements to the latitude of 45°, and to sea-level. The stand- 
ard thermometer should then have its boiling and freezing points determined 
under, or reduced to such conditions. The value of g, the acceleration due 
to gravity, is, at Paris, latitude 48° 50' 14'' and 60 metres above sea-level, 
9.809218 metres; and at 45°, and at sea-level, it is 9.806056 metres. Con- 
sequently, 760 mm. of mercury at 45° gives a pressure equal to that of 
759.755 mm. at Paris ; and this corresponds to a temperature of 99.°991 C. 

In other words, the thermometer which is standard at 45° has each degree 
0.99991 of the length of the degree of a thermometer standard at Paris. 

To reduce Equation B to 45° latitude, we have 

and for Equation (7, 

logp = a + log ll^'llll - ba^'-^'^-'^^ + c^(o-9^"-i«» 

= a + lOO" ^^^'^^^^ _ 5(j -0.009 ^0.99991 (« - 100) _^ ^O- 0.009 00.99991 («- 100)^ 

The resulting equations which were used in calculating Table III are 

B. For steam from 0° to 100° C. at 45° latitude. 

log p = a^- ha^ -h cp^^, 

ctj = 4.739502. 
log 6 = 0.6117400. 
log c = 8.13204 - 10. 
log ttj = 9.996725828 - 10. 
log/?! = 0.0068641. 

n ■= t, 

C. For steam from 100° to 220° C. at 45'' latitude. 

log p = a,- 6iai" -{- Ci/3i«. 

tti = 5.457570. 
log 6i = 0.4120021. 
log q = 7.74168 - 10. 
log aj - 9.997411296 - 10. 
log/?i = 0.0076418. 

n = t - 100. 



SATUBATEB STEAM, AND OTHER VAPOBS. 9 

Pressure of Steam at Latitude 45°. — English System. — To reduce the 
equations for the pressure of steam, so that they will give the pressures in 
pounds on the square inch for degrees Fahrenheit, there are required the com- 
parison of measures of length, and of weight, the comparison of the scales 
of the thermometers, and the specific gravity of mercury. 

Professor Rogers {Proceedings of the Am. Acad, of Arts cind Sciences, 
1882-83, also Additioncd Observations, etc.) gives for the length of the metre, 
39.3702 inches. This differs from the value given by Capt. Clarke {Pro- 
ceedings of the Poycd Society, vol. xv., 1866), by an amount that does not 
affect the values in the tables ; his value being 39.370432 inches. 

Professor Miller {Phil. Transactions, cxlvi., 1856) gives for the weight 
of one kilogram, 2.20462125 pounds. 

Regnault gives, for the weight of one litre of mercury, 13.5959 kilograms. 
The degree Fahrenheit is |- of the length of the degree Centigrade. 

^ , , 13.5959 X 2.204621 
Let k= s ; 



39.3702 
then the equations B and C have for the reduction to degrees Fahrenheit, 
and pounds on the square inch, 

log p = Cfj + log k — ha^ + c^^, 

log p = a^-^ log k - h^a^ + c, /5i^. 

The resulting equations, which were used in calculating Tables I and II, 
are : — 

B. For steam from 32° to 212° F., in pounds on the square inch. 

logp = a., - ha.^ + c^/. 

0,2 = 3.025908. 
log h = 0.6117400. 
log c = 8.13204 - 10. 
log ttg = 9.998181015 - 10. 
log^S^ = 0.0038134. 

n = t — 32. 

C. For steam from 212° to 428° F., in pounds on the square inch. 

logp = a^ - b^a^^ +c^P^' 

a^ = 3.743976. 
log 6i = 0.4120021. 
log Cj = 7.74168 - 10. 
log a^ = 9.998561831 - 10. 
log/32 = 0.0042454. 
n = t - 212. 
All of the foregoing equations make the pressure a function of the tem- 
perature on the scale of the air-thermometer. It will be assumed that the 
difference between that scale and the absolute scale may be neglected. 



10 



SATUEATED STEAM, AND OTHER VAPOBS. 



Other Equations for the Pressure of Steam. — Kankine, in his Steam 
Engine and other Prime Movers^ gives the following equation : — 



logi> 






For pounds on the square inch, corresponding to degrees Fahrenheit, — 

A = 6.1007. 
log B = 3.43642. 
log C = 5.59873. 

T = t + 461.°2F. 

This equation has been largely used for calculating tables on the English 
system. The following table will give a comparison between the results from 
this formula and those from Formulae B and C. 



TEMPERATUKE. 


PEESSURE. 






Repnault at 45° latitude. 


Rankine. 


32 


0.0890 


0.083 


77 


0.4555 


0.452 


122 


1.7789 


1.78 


167 


5.579 


5.58 


212 


14.99 


14.70 


257 


33.711 


33.71 


302 


69.27 


69.21 


347 


129.79 


129.8 


392 


225.56 


225.9 


428 


336.26 


336.3 



Differential Co-efficient — . — As will be seen later, the differential 

dt 

co-efficient — is used in calculating the volume and density of saturated 

vapors. 

From the general equation of the form, 

log p = a + 6a" -f C)8", 
differentiation gives 

in which M is the modulus of the common system of logarithms. 
The equation may be written, — 

p dt 
The calculation of the values of the constants gives the following results 
for latitude 45° : — 



SATURATED STEAM, AND OTHER VAPORS. 11 

French units. 

B, For 0° to 100° C, mm. of mercury, 
log A = 8.8512729 - 10. 
log B = 6.69305 - 10. 
log aj = 9.996725828 - 10. 
log (3^ = 0.0068641. 
0. For 100° to 220° C, mm. of mercury, 
log A = 8.5495158 - 10. 
log B = 6.34931 - 10. 
loga^ = 9.997411296 - 10. 
log ygj = 0.0076418. 

English units. 

B, For 32° to 212° F., pounds on the square inch. 

log A = 8.5960005 - 10. 
log S = 6.43778 - 10. 
log ag = 9.998181015 - 10. 
log /?^ = 0.0038134. 

C. For 212° to 428° F., pounds on the square inch, 

log A = 8.2942434 - 10. 
log B = 6.09403 - 10. 
log ttg = 9.998561831 - 10. 
log ^2 = 0.0042454. 

Heat of the Liquid and Specific Heat. — A preliminary series of experi- 
ments convinced Regnault that the specific heat of water at low temperature 
is unity. To test the specific heat at higher temperatures, he ran hot water 
from a boiler, and at a known temperature, into a calorimeter in which the 
temperature varied from 8° to 14° C, and the resulting upper temperature 
varied from 17° to 29° C. Knowing the original weight of water in the 
calorimeter, the weight run in from the boiler, and the initial and final 
temperatures in the calorimeter, he calculated the mean specific heat of water 
between the temperature of the boiler and the final temperatures of the 
calorimeter. A series of forty such experiments was made, with the tem- 
perature of the boiler varying from 108° to 192° C, from which Regnault 
concluded that the mean specific heat from 0°to 100° is 1.005 ; and from 0° to 
200°, 1.016. The corresponding heat of the liquid, i.e., the heat required 
to raise one kilogram of water from 0° to a given temperature, t, is 

For 100° . . . . 100.5 
200° .... 203.2 

Assuming an equation of the form 

q = t -{- Ae + Bi^, 



12 SATURATED STEAM, AXD OTHER VAPORS. 

and solving for the two constants b}^ aid of the two known values of q, the 
following equation, which is commonly used, is deduced : — 
q = t '\- 0.00002^2 _^ 0.0000003?^ 
The specific heat at am- temperature is, therefore, — 

c = ^^ = 1 + 0.00004f + O.OOOOOOi^ 

These equations are for use with the Centigrade scale ; for the Fahrenheit 
scale, a given temperature may be reduced to the Centigrade scale, and then 
introduced in the same equations. 

The process of making the experiments is really a complex one ; for the 
water, in leaving the boiler, has work done on it by the steam pressure in 
the boiler, and it has a certain velocity impress on it at the same time, and 
again, in entering the calorimeter, it does work against the atmospheric 
pressure, and the kinetic energy of its motion is changed into heat. At 
higher temperatures there is a double change of state ; part of the water 
changes to steam on leaving the boiler, and that steam is condensed again in 
the calorimeter. It is probable that the error of neglecting the effect of these 
sevei-al actions is inconsiderable. 

The degree of accuracy to be accorded to this work is indicated b}' the 
fact that Re^nault sfives four sisfnificant fii^ures in stating the data for 
the calculation of the constants in the equations. 

Rowland's Experiments. — A series of experiments was made b}- Rowland 
at Baltimore, to determine the mechanical equivalent of heat, which gave a 
delicate method of determining the heat of the liquid, and the specific heat. 

The apparatus used was similar to that used by Joule, with modifications 
to give greater certaint}' of results. The calorimeter was of larger size, and 
the paddle had the upper vanes curved like the blades of a centrifugal pump, 
to give a strong circulation up through the centre, past the thermometer for 
taking the temperatures, and down at the outside. The paddle was driven 
by a petroleum engine, and the power applied was measured b}" making the 
calorimeter into a friction brake, with two arms at which the turning moment 
was measured. Radiation was made as small as possible, and then was made 
determinate by use of a water-jacket outside of the calorimeter. 

The experiments consisted essentially in delivering a measured amount of 
work to the water in the calorimeter, and in noting the rise of temperature 
produced thereby. 

The whole range covered by the experiments was from 2° to 41^ C. The 
results show that 430 kilogrammetres of work are required to raise one kilo- 
gramme of water from 2° to 3° C. Assuminsj that the same amount will be 
required to raise the same weight from 0° to 1° and from 1° to 2°, the follow- 
ing table has been arranged from Rowland's final table of results : — 



SATURATED STEAM, AXD OTHER VAPORS. 
ROWLAND'S MECHANICAL EQUIVALENT OF HEAT. 



13 



6 

i 

2 

1 


P-Z5 




5.1 
HI 
iSS 


m 




li 

.0=3 s 


■5 = 




=.- — ii 

c ~ 3 

pi 


1 


430 




1.0068 


1.007 


22 


9424 


426.1 


22.065 


22.063 


2 


860 


_ 


2.0135 


2.014 


23 


9850 


426.0 


23.063 


23.061 


3 


1290 


_ 


3.0204 


3.022 


24 


10277 


425.9 


24.062 


24.059 


4 


1721 


_ 


4.0295 


4.029 


25 


10701 


425.8 


25.055 


25.058 


5 


2150 


429.8 


5.0339 


5.036 


26 


11128 


425.7 


26.054 


26.053 


6 


2580 


429.5 


6.0408 


6.040 


27 


11553 


425.6 


27.050 


27.048 


7 


3009 


429.3 


7.0452 


7.045 


28 


11978 


425.6 


28.045 


28.042 


8 


3439 


429.0 


8.0520 


8.049 


29 


12399 


425.5 


29.031 


29.037 


9 


3868 


428.8 


9.0564 


9.054 


30 


12828 


425.6 


30.035 


30.032 


10 


4296 


428.5 


10.059 


10.058 


31 


13253 


425.6 


31.030 


31.027 


11 


4723 


428.3 


11.058 


11.060 


32 


13675 


425.6 


32.018 


32.023 


12 


5151 


428. 1 


12.061 


12.061 


33 


14101 


425.7 


33.016 


33.018 


13 


5578 


427.9 


13.060 


13.063 


34 


14527 


425.7 


34.011 


34.014 


14 


6006 


427.7 


14.063 


14.064 


35 


14952 


425.8 


35.008 


35.009 


15 


6433 


427.4 


15.065 


15.066 


36 


15379 


425.8 


36.008 


36.007 


16 


6861 


427.2 


16.064 


16.066 


37 


15805 


_ 


37.007 


37.005 


17 


7289 


427.0 


17.066 


17.066 


38 


16231 


- 


38.003 


38.004 


18 


7717 


426.8 


18.068 


18.066 


39 


16657 


- 


39.000 


39.002 


19 


8144 


426.6 


19.068 


19.066 


40 


17083 


- 


39.998 


40.000 


20 


8571 


426.4 


20.068 


20.066 


41 


17508 


_ 


40.993 


_ 


21 


8997 


426.2 


21.065 


21.064 













In the above table, column 1 gives the number of degrees above freezing 
on the Centigrade scale ; column 2 gives the number of kilogrammetres 
required to raise one kilogramme of water from freezing point to the given 
temperature ; column 3 is Rowland's mechanical equivalent of heat at the 
given temperature derived from 10° intervals on column 2 ; column 4 is 
obtained by dividing the numbers in column 2 by the mechanical equivalent 
of heat at 16f° C, or 62° F., from column 3 ; and column 5 is calculated by 
considering the specific heat to be constant for each five degrees of tempera- 
ture. These specific heats were derived from a curve obtained by plotting 
temperatures for abscissae, and heats of the liquid for ordinates. The values 
of the specific heats will be given later, in connection with those for higlier 
temperatures. 

A review of the preceding table shows that the specific heat at low tem- 
peratures varies quite markedly, so thxit it appeared advisable to investigate 
the effect of this variation on Regnault's experiments already quoted. 
This was done quite expeditiously by multiplying the mean specific heat given 
by him for his several experiments by the true average specific heat for the 
range of temperature in the calorimeter. This corrected specific heat was 
then used to calculate the increase of heat from the final temperature of the 
calorimeter to the temperature of the boiler, and that increase was added to 
the heat of the liquid from the table to find the heat of the liquid at the 



14 



SATURATED STEAM, AND OTHER VAPORS. 



temperature of the boiler. The results were then plotted as before, and 
compared with the heats of the liquid derived from Regnault's mean specific 
heats uncorrected. The points by the corrected method were a little more 
regularly arranged than the points obtained by assuming the specific heat to 
be unit}" at low temperatures ; but the improvement was inconsiderable. The 
inequality of the specific heat at low temperatures is seldom so much as the 
unavoidable errors of the method. 

It appeared, that if the specific heat was assumed to be constant, from 
40° to 45°, from 45° to 155°, and from 155° to 200° C, the straight lines thus 
drawn represented the experimental values as recalculated quite nearly ; and, 
further, they represented the uncorrected experimental values more nearly 
than Regnault's equation. 

Specific Heat of Water. — The combination of Rowland's and Regnault's 
experiments on the heat of the liquid by the method described gives the 
specific heats set down in the following table, Centigrade scale : — 

SPECIFIC HEAT. 

1.0072 

1.0044 

1.0016 

1. 

0.9984 

0.9948 

0.9954 

0.9982 

1. 

1.008 

1.046 

Thermal Unit. — Heat is measured in calories, or British thermal units 
{BTU). A calorie commonly is defined as the heat required to raise one 
kilogramme of water from freezing point to 1° C. ; and a British thermal 
unit, that required to raise one pound from 32° to 33° F. Nothing is known 
about the specific heat of water from 0° to 2° C. ; consequently the commonly 
accepted value of the thermal unit is an ideal quantity inferred from the 
behavior of water at higher temperatures. It is more scientific to take an 
easily verified quantity for the standard ; and there is a practical convenience 
in choosing 62° F. for the standard temperature, because it is near the mean 
temperature of the air during experimental work. Therefore, it is near the 
mean temperature in the calorimeter during ordinary work with that instru- 
ment ; and the specific heat of water for the range of temperature in the 
calorimeter may usually be considered to be unity without error, unless great 
refinement is desired. 

The BTU in Tables I and II is taken to be the heat required to raise 



From 0° to 


5°C. 


32° to 


4P 


5° 


10° 


41° 


50° 


10° 


15° 


50° 


59° 


15° 


20° 


59° 


68° 


20° 


25° 


68° 


77° 


25° 


30° 


77° 


86° 


30° 


35° 


86° 


95° 


35° 


40° 


95° 


104° 


40° 


45° 


104° 


113° 


45° 


155° 


113° 


311° 


155° 


200° 


311° 


392° 



SATURATED STEAM, AND OTHER VAPORS. 



15 



one pound of water from 62° to 63° F. This agrees substantially with the 
definition of the calorie, as the heat required to raise one kilogramme of 
water from 15° to 16° C. 

In the tables for other vapors than steam, the old definition for the calorie, 
and Eeguault's value for the heat of the liquid, are retained, to avoid entire 
recalculation. 

Mechanical Equivalent of Heat. — The mechanical equivalent in metre- 
kilogrammes of one calorie at 16f° C, deduced from Rowland's experiments 
in the third column of the table on page 58, is 427.1. 

Since the value given by Joule is commonly quoted, it will be of interest 
to make a comparison of his latest work (1873) with Rowland's, as given in 
the following table : — 



Temperature. 


Joule's Value at 

Manchester, 
English System. 


Reduced to the Air Thermometer 
and to the latitude of Baltimore. 


Rowland's Value, 
corresponding. 


English. 


French. 


14.7° 
12.7° 
15.5° 
14.5° 
17.3° 


772.7 
774.6 
773.1 
767.0 
774.0 


776.1 

778.5 

776.4 

770.5 

' 777.0 


425.8 
427.1 
426.0 
422.7 
426.3 


427.6 
428.0 
427.3 
427.5 
426.9 



The value of g at Baltimore, latitude 39° 17', is 980.05 centimetres there- 
fore, reducing to 45° of latitude, and at the sea level, the value of the 
mechanical equivalent of heat is 
J" =426.9. 

To reduce to the English system, multiply by f, and by the length of the 
metre in feet, so that 

J = 778. 

Total Heat. — This term is defined as the heat required to raise a unit of 
weight of water from freezing point to a given temperature, and to entirely 
evaporate it at that temperature. The experiments made by Regnault were 
in the reverse order ; that is, steam was led from a boiler into the calorimeter, 
and there condensed. Knowino^ the initial and final weights of the calori- 
meter, the temperature of the steam, and the initial and final temperatures 
of the water in the calorimeter, he was able, after applying the necessary 
corrections, to calculate the total heats for the several experiments. 

As a conclusion of the work, he gives the following values for the total 



heats : — 










10° 


610 


By equation, 609.6 




63° 


625 


625.2 




100° 


637 






195° 


666 





16 SATURATED STEAM, AND OTHER VAPORS, 

Assumiog an equation of the form 
X = A -^ Bt, 

Regnault calculated the constants from the values given for 100° and 195°, 
and gives the equation 

A = 606.5 + 0.305^ 
Wishing to see the effect of the var^^ing value of the specific heat at low 
temperatures, I recalculated the total heats given by experiment, by a method 
resembling that used in recalculation of the heats of the liquid, and plotted 
the results together with Regnault's values uncorrected. The recalculated 
points were a little more regular than the original ones, and lay nearer the 
line represented by the above equation. Especiall}^ did the recalculated 
points for those experiments, for which the true mean specific heat of the 
water in the calorimeter was nearly unity, lie near that line. It therefore 
appears that the equation represents our best knowledge of the total heat of 
steam. 

For the Fahrenheit scale the equation becomes 

X = 1091.7 + 0.305 {t - 32). 
Heat of Vaporization. — If the heat of the liquid be subtracted from the 
total heat, the remainder is caUed the heat of vaporization, and is represented 
by r, so that 

r = X — q. 
Internal and External Latent Heat. — The heat of vaporization overcomes 
external pressure, and changes the state from liquid to vapor at constant 
temperature and pressure. Let the specific volume of the saturated vapor be 
s, and that of the liquid be cr, then the change of volume is s — a- = u, on 
passing from the liquid to the vaporous state. The external work is 

p{s — (t) = pu, 
and the corresponding amount of heat, or the external latent heat, is 

Ap{s — 0-) = Ajm, 
A being the reciprocal of the mechanical equivalent of heat. 

The heat required to do the disgregation work, or the internal latent 
heat, is 

p = r —Aim. 
Specific Volume and Density of Steam. — On account of the great diflSculty 
of direct determination of the weight of saturated steam, it is customar}- to 
calculate the specific volume of steam by aid of the following equation, 
derived by the application of the principles of thermo-dynamics to the general 
equation representing the properties of saturated vapor : — 

r 1 ^ 
'^Af'dp^''^ 
dt 



SATURATED STEAM, AND OTHER VAPORS. 17 

in which A is the reciprocal of the mechanical equivalent of heat, T is the 

temperature from the absolute zero, and o- is the volume of one unit of weight 

dp 
of the liquid from which the vapor is formed. The differential co-efficient -j- 

can be calculated by aid of the equations on page 11. 

The absolute temperature is obtained by adding 273.7 to the temperature 
in degrees Centigrade, or 4G0.7 to the temperature in degrees Fahrenheit. 

The volumes and densities of saturated steam given in Tables I, II, 
and III, were calculated by this method. 

It is of interest to consider the degree of accuracy that may be expected 
from this method of calculating the density of saturated vapor. The value 
of ?• repends on A, and q; for the first, Eegnault gives three figures in the data 
from which the empirical equation is deduced, and the experimental work 
does not indicate a greater degree of accuracy. The fourth figure, if stated, 
is likely to be in error to the extent of five units. The value of T is com- 
monly stated in four figures, of which the last may be in error by two units. 
A, as determined by Rowland, has four figures, the last being uncertain to 

dp 
the extent of one or two units. The differential co-efficient --- is deduced 

dt 

from the equations for calculating p; and those equations are derived from 

data liaving five places of significant figures. Now the Equations B and (7, 

for steam at 45° of latitude for the English system give a pressure of 14.6967 

pounds on the square inch ; but the specific volume calculated by aid of 

Equation B is 26.550 cubic feet, while Equation C gives 26.637 cubic feet. 

The mean, 26.60, differs from either extreme by about one in seven hundred. 

This discrepancy is due to the fact that the curves represented by Equations 

B and C meet at the common temperature, 212°, but do not have a common 

tangent. Since the equations are empirical and not logical, the error or 

uncertainty is unavoidable, and all calculated specific volumes are affected by 

a similar uncertainty. The greatest probable error is in determining ?% for 

which it may be about one in one thousand. The error introduced into this 

equation by using the values of A in common use, that is, 772 instead of 778, 

is about one in one hundred. 

Tate and Fairbairn's Experiments. — In 1860 an attempt was made by 
Tate and Fairbairn to determine the specific volume of steam by direct 
experiment. The following table, taken from the PhUosopJiiccd Transactions, 
Vol. d., gives the results of all their experiments, together with the volumes 
calculated by their empirical formula, 



18 



SATURATED STEAM, AND OTHER VAPORS. 





Pressure in 


ilaximum 


Specific 


Specific 






Inches 


Temperature, 


Volume from 


Volume from 


Error of 




of Mercury. 


Fahrenheit, of 


Experiments. 


Formula. 


Formula. 




P. 


Saturation. 
T 


V. 


V. 




1 


5.35 


136.77 


8275.3 


8183 


—9-0- 


2 


8.62 


155.33 


5333.5 


5326 


-ih 


3 


9.45 


159.36 


4920.2 


4900 


— tU 


4 


12.47 


170.92 


3722.6 


3766 


+-rf 


5 


12.61 


171.48 


3715.1 


3740 


+ TT^ 


6 


13.62 


174.92 


3438.1 


3478 


+ h 


7 


16.01 


182.30 


3051.0 


2985 


-i 


8 


18.36 


188.30 


2623.4 


2620 


+ «14 


9 


22.88 


198.78 


2149.5 


2124 


-i^ 


V 


53.61 


242.90 


943.1 


937 


-T+T 


2' 


55.52 


244.82 


908.0 


906 


-tC 


S' 


55.89 


245.22 


892.5 


900 


+ TiT 


4' 


66.84 


255.50 


759.4 


758 


-yJi 


o' 


76.20 


263.14 


649.2 


669 


+-A 


6' 


81.53 


267.21 


635.3 


628 


-i- 


r 


84.20 


269.20 


605.7 


608 


+m 


8' 


92.23 


274.76 


584.4 


562 


— 'h 


9' 


90.08 


273.30 


543.2 


545 


+ ^fT 


10^ 


99.60 


279.42 


515.0 


519 


+ Ti« 


IV 


104.54 


282.58 


497.2 


496 


-T^T 


12' 


112.78 


287.25 


458.3 


461 


+ 3^ 


13' 


122.25 


292.53 


433.1 


428 


—h 


14' 


114.25 


288.25 


449.6 


456 


+rf 



It is apparent that the errors of this formula are much larger than the 
probable errors of the thermo-chnamic method. 

The following table, giving the volumes in cubic metres of one kilogramme 
of saturated steam, shows the comparison of the two methods ; — 

B}^ equation o" c. 50° c. loo' c. lao" c. 200° c. 

'^^ -h o- . . 211.5 12.11 1.660 0.3875 0.1277 



dt 



V ^ 
^ ~ at' dp 

From equation 

F= 25.62 + 



49153 
P + 0.72' 



54.97 11.43 1.643 0.3706 0.1343 



Steam Entropy. — From the second law of thermo-dynamics may be 
deduced the equation 

in which </> is the entropy, dQ is the heat applied or withdrawn, and T is the 
absolute temperature. Since the entropy depends on the state of the sub- 
stance onl3% and not on the method of arriving at that state, we may calculate 
the increase of entropy in one unit of weight of a given mixture of water 
and steam, above the entropy of one pound of water at freezing point, in the 
following method. Suppose that one unit of weight of water is raised from 



SATURATED STEAM, AND OTHER VAPORS. 19 

freezing point to the temperature t, and that the portion x is then changed 
into steam. During the first operation the change of entropy will be 

e= r '^^ = r — 

Jo T Jo T' 

During the second operation the change of entropy will be 

xr 

since the heat is added at the constant temperature t. The entire change of 

entropy will be 

xr r cdt xr 

At any other state the entropy of a unit of weight of a mixture of steam 
and water will be 

and the change of entropy will be 

<^ - <^i = f + ^ - ^ - ^r 

During an adiabatic change no heat is transmitted, and the entropy is 
constant. 

... ^ + = ^ + 6^. 

When the initial state including the value of x is known, and also the 
final temperature or pressure, the final value of x^ maj^ be calculated by 
the above equation ; and the initial and final volumes may be found by the 
equations 

V = xu -{- cr, v^ = x^u^ -\- (T ; 

the value of u for a given temperature or pressure, from the equation, 

s = u -\- a-. 
Entropy of the Liquid. — When the specific heat of a liquid is known in 
terms of the temperature, the entropy of the liquid. 



e 



~ jo ~T' 



is readily calculated. For water we have, for example, the entropy of the 
liquid at 13° C. 

1.0072 log, ^^ + 1.0044 log, ^ + 1.0016 log, ^. 

For other liquids having the general formula for the heat of the liquid, 

q = at + hf + c^% 

the entropy is 

+ 2>cf) dt 



rt (g + 2bt + 
^ = jo T 



20 



SATURATED STEAM, AND OTHER VAPORS. 



Other Vapors. — Tables IV to IX are taken from Zeuner's MechaniscJien 
Wdrmetheorie. His values for the specific volume and density were calcu- 
lated with 273 for the absolute temperature of 0° C, and with 424 for the 
mechanical equivalent of heat. To bring these tables into accord with Tables 
I, II, and III, the values of the specific volume and density have been 
modified by using 273.7 for the absolute temperature of 0° C, and 426.7 for 
the mechanical equivalent of heat at Paris. 

The equations by which the tables were calculated, taken from Regnault's 
memoirs, Academie cles Sciences^ Comptes rendus, Tome XXXVI, are here 
assembled, together with Zeuner's equations for the differential co-efficient, 

1 ^!l 

p dt 

TEMPERATURE AKD PRESSURE. 





log p= [ 


a 


b 


c 


1 


2 


3 


4 


5 


Alcohol 


a — ha^ + c/?" 


5.4562028 


4.9809960 


0.0485397 


Ether 


a + ba^ — c/S" 


5.0286208 


0.0002284 


3.1906390 


Chloroform .... 


a — ha^ — c/^n 


5.2253893 


2.9531281 


0.0668673 


Carbon bisulphide . 


a — ban — f.j3n 


5.4011662 


3.4405663 


0.2857386 


Carbon tetrachloride . 


a — ba^ — c/3" 


12.0962331 


9.1375180 


1.9674890 



TEMPERATURE AXD PRESSURE ~ ConcZi/(Zc(Z. 





log a. 


log p. 


n 


Limits. 




6 


7 


8 


9 


Alcohol 


1.99708557 


1.9409485 


t + 20 


-20°, + 150°C. 


Ether 


0.0145775 


1.996877 


t+20 


-20°, + 120° 


Chloroform .... 


1.9974144 


1.9868176 


t-20 


+20°,+ 164° 


Carbon bisulphide 


1.9977628 


1.9911997 


t+20 


-20°, + 140° 


Carbon tetrachloride . 


1.9997120 


1.9949780 


t+20 


-20°, + 188° 



The equation for the temperature and pressure of the satui'ated vapor of 
aceton, as recalculated by Zeuner, is, — 



log p = a — 6a'' -h c^. 

a = 5.3085419. 
log haJ" = -f 0.5312766 - 0.0026148f. 
log c^ = - 0.9645222 - 0.0215592^ 



SATUBATED STEAM, AND OTHER VAPOBS. 
1 dp 
From Zeuner's Wdrmeiheorie. 



21 





Sign. 


Log (Aa") 


Log (^,3") 


^a" 


^3« 


Alcohol . . . , 

Ether 

Chloroform . . . 
Carbon bisulphide . 
Carbon tetrachloride, 
Aceton 


+ 
+ 

+ 
+ 
+ 


+ 
+ 
+ 
+ 
+ 


— 1 . 1720041 —0. 0029143^ 
—1.3396624— 0.0031223i 
-1.3410130— 0.0025856i 
-1.4339778-0.0022372^ 
— 1.8611078-0. 0002880^ 
-1. 3268535 -0.0026148^ 
t, temperature C- 


-2.9992701-0.0590515^ 
—4. 46 16396 + 0. 0145775^ 
-2.0667124-0.0131824^ 
-2.051 1078-0. 0088003^ 
-1.3812195-0.0050220^ 
-1.9064582-0.0215592^ 



Alcohol 

Ether 

Chloroform 

Carbon bisulphide 

Carbon tetrachloride 

Aceton 



Ether 
Chloroform 
Carbon bisulphide 
Carbon tetrachloride 
Aceton 



HEAT OF THE LIQUID, 

q = 0.54754f + 0.0011218^2 _^ 0.000002206i^ 

q = 0.52901^ + 0.0002959^2 

q = 0.23235^ + O.OOOOoOTi^ 

q = 0.23523^ + 0.0000815^^ 

q = 0.19798^ + 0.0000906^^ 

q = 0,50643i + 0.0003965^2 

TOTAL HEAT. 

A = 94 + 0.45^ - 0.00055556^2 
X = 67 -\- OASlDt 
A = 90 + 0.1460U - 0.0004123^2 
A = 52 4- 0.14625^ - 0.000172^2 
A = 140.5 + 0.36644^ - 0.000516^2 



The total heat of alcohol varies in so irregular a manner that no equation 
can be given for it. 

Zeuner gives the following empirical equations for calculating the heat 
equivalent of the internal work, which are proposed to lessen the labor of 
calculation. 

HEAT EQUIVALEiS^T OF I^^TERNAL WORK:. 



Water 

Ether 

Chloroform 

Carbon bisulphide 

Carbon tetrachloride 

Aceton 



p = 575.40 
p = 86.54 - 
p = 62.44 - 
p - 82.79 - 
p = 48.57 - 



- 0.79U 

0.10648^ - 0.0007160^2 
0.11282^ - 0.0000140^2 
0.11446« - 0.0004020^2 
0M8Ut - 0.0002080^2 



131.63 - 0.20184f - 0.0006280^2 



Sulplmr Dioxide and Ammonia. — The use of ice-machines has brought 
into prominence liquids which vaporize at low temperatures. For two such 
liquids, sulphur dioxide and ammonia, Regnault gives the following equations 
for temperature and pressure : — 



22 SATUBATED STEAM, AND OTHER VAPORS. 

SULPHUR DIOXIDE. AMMOXIA. 

log p = a — 6a" — c/3* log p = a — ha!" — c(3^ 

a = 5.6663790 a = 11.5043330 

h = 3.0146890 6 = 7.4503520 

c = 0.1465400 c = 0.9499674 

log a = 1.9972989 log a = 1.9996014 

log /3 = 1.9872900 log ;8 = 1.9939729 

n = i + 28 n = t -\- 22 

Limits, —28, +62. Limits, —22, +82. 

Unfortunately, the heat of the liquid and the total heat for these sub- 
stances have not been determined. Tlie following approximate method of 
determining those quantities, and calculating tables, has been proposed by 
Ledoux, Annales des Mines, 1875. 

Zeuner has shown that the properties of superheated steam may be 
represented by an equation having the form 

pv = BT — Cp"", 
in which 

Cp being the specific heat of superheated steam at constant pressure. C and 
n are constants to be determined from the properties of the substance. 
Using 273 for the absolute temperature of freezing point, and 424 for the 
mechanical equivalent of heat, Zeuner deduces the following values for 
the constants in the above equation, when the pressure is expressed in kilo- 
grammes per square metre : — 

B = 50.933 C = 192.5 n = f. 

The equation has been shown to represent the properties of superheated 
steam near the point of saturation, and also the properties of dry saturated 
steam, quite well. 

Ledoux assumes that similar equations ma}^ be deduced to represent 
the properties of the vapors of sulphur dioxide and ammonia, founded on 
Regnault's experiments on the compressibility of gases and vapors, and on 
the co-eflficient of dilatation. Since the co-efficient of dilatation for vapor 
of ammonia is not given by Regnault, he assumes it to be 0.0039, that 
for sulphur dioxide being 0.0039028. 

The constants deduced for the equations are, — 

SULPHUR DIOXIDE. AMMONIA. 

B = 13.882 B = 52.4943 

C = 3.8455 C = 43.7144 

n = 0.44487 n = 0.32685 

These equations he uses for calculating the specific volume and density 



SATURATED STEAM, AND OTHER VAPORS. 23 

of the saturated vapors. The total heat is deduced from the adiabatic equa- 
tions of a superheated vapor. To obtain the heat of vaporization, the 
equation . 

u dt 

is combined with the equation for a superheated vapor. Thus all the elements 
are assembled for the calculation of tables of the properties of the saturated 
vapors. For convenience, empirical equations having the same form as the 
equations used to represent Regnault's experiments on the total heat and 
the heat of the liquid are given. They are as follows : — 

SULPHUR DIOXIDE. 

Apu = 8.243 - 0.0196^ - O.OOOllGi^ 
r = 91.396 - 0.236U - 0.000135^2 

A = 91.396 -f 0.12723^ - 0.000131^2 

q = 0.36333^ + 0.00004^^ 

c = 0.36333 + 0.00008^ 

AMMONIA. 

Apu = 30.154 + 0.0886U - 0.000059^2 
r = 313.63 - 0.6250^ - 0.002111^2 
A = 313.63 + 0.3808^ - 0.000282^2 
q = 1.0058^ + 0.001829^2 
c = 1.0058 + 0.003658^ 
Finally, Ledoux gives the following equation to represent the pressure in 
kilogrammes per square metre, to take the place of Regnault's equations 
quoted on p. 22 : — 

t 

p =aa^-'"^ 

SULPHUR DIOXIDE. AMMONIA. 

a = 15840 a = 43474.64 

log a = 4.1991752 log a = 4.6382260 

a = 1.04135 a = 1.0386605 

log a = 0.0176387 log a = 0.0164736 

m = 0.0043129 m = 0.0040112 

Tables X and XI were calculated by aid of the equations written, and 
may be of use for approximate calculations, in default of more reliable tables. 
Specific Volume of Liquids. — Table XII was taken from the Phys.-Chem, 
Tahellen of Landolt and Bornstein. 

Volume of Water. — Table XIII gives the volumes of water compared 
with its volume at 4°. From 0° to 100° C, the values are those given by 
Rossetti. Above 100°, the values are those calculated by the equations given 
by Hirn in the Annales de Chimie et de Physique^ 1867. 

Volumes of Liquids. — The volumes of liquids at high temperatures, com- 



24 



SATURATED STEAM, AND OTHER VAPORS. 



pared with the volume of water at 4° C, are represented by the following 
equations given by Hirn in the Annates : — 



Water 100° C. to 200° C. (vol. at4°C.= Logs. 

unity) v = l+0.00010867875i 6.0361445-10 

+0.0000030073653^2 4.4781862-10 

+0.0000000028730422^3 1.4583419-10 

—0.0000000000066457031^4 8.8225409-20 

Alcohol 30° C. to 160° C. (vol. at 0° C.= 

tuiity) j;=l+0.00073S92265« 

+0.00001055235f2 
—0.000000092480842^3 

+ 0. 0000000004041 3567^* 
Ether 30° C. to 130° C. (vol. at 0° C.= 

unity) r=l+0.0013489059i 

+0.0000065537^2 
—0.000000034490756^3 
+ 0. 00000000033772062^4 

Carbon bisulphide 30° to 160° C. (vol. at 

0°C.=unity) r=l+0.0011680559i 

+0.0000016489598^2 

-0.00000000081119062^3 

+0.000000000060946589^4 

Carbon tetrachloride 30° to 160° C. (vol. at 

0°C.=unity) r=l+0.0010671883« 

+0.0000035651378^2 
— 0.00000001494928U3 
+0.000000000085182318^4 



6.8685991-10 
3.0233492-10 
2.9660517—10 
0.6065278-10 

7.1299817-10 
4.8164806-10 
2.5377028-10 
0.5285571-10 



7.0674636-10 
4.2172103—10 
0.9091229-10 
1.7849494-20 



7.0282409-10 
4.5520763-10 
2.1746202-10 
1.9303494—20 



Other Data. — For convenience the following data are assembled : — 

f 39.3702 (Rogers) 



Length of the metre in inches . 

Weight of the kilogramme in pounds . 
Weight of 1 litre (1 cu. decimetre) of mercury 
One horse power, in foot pounds per second 
Cheval iX vapeur, in kilogrammetres per second 

Normal pressure of the atmosphere . 



39.370432 (Clarke) 

2.20462125 

13.5959 kilos. 

550 

75 

760 mm. of mercury. 

10,333 kilos per sq. m. 

14.6967 lbs. per sq. in. 

2116.32 lbs. per. sq. ft. 

273.°7 C. 
, 492.°7 F. 

Explanation of the Tables. — In Table I, the first column gives the tem- 
perature, t, of saturated steam. 

The second column gives the corresponding pressure, p, in pounds on the 
square inch, above an absolute vacuum ; the differences are placed between 
the two numbers from which they are derived. For example, the pressure 
at 40° F. is 0.1216 pounds per square inch ; and the difference to be used in 
interpolation, and placed half a line lower, is 48. 



Absolute temperature of freezing point 



SATURATED STEAM, AND OTHER VAPORS. 25 

The third column gives the heat of the liquid, g, required to raise the 
temperature of one pound of water from 32° F. to a given temperature. 

The fourth column gives the total heat, A, required to raise one pound of 
water from 32° F. to a given temperature, and to entirely vaporize it under 
the pressure due to that temperature. 

The fifth column gives the heat of vaporization, or the heat required to 
vaporize one pound of water at a given temperature, under the pressure 
corresponding. 

The sixth column gives the heat required to do the disgregation work 
during the vaporization of one pound of water. 

The seventh column gives the heat required to overcome the external 
pressure, and do the work of increasing the volume from a to s. 

The eighth column gives the entropy of the liquid. 

The ninth and tenth columns give the specific volume, or volume in cubic 
feet, of one pound of saturated steam, and the density or weight of one 
cubic foot in pounds. 

Table II differs from Table I in that it is arranged to give the properties 
of saturated steam for each pound of pressure. 

Table III gives the properties of saturated steam in French units ; and 
Tables IV to XI give the properties of other saturated vapors in the same 
units. It is to be noted that the pressures in Tables IV to IX are in milli- 
metres of mercury ; in Tables X and XI, are in kilogrammes per square 
metre. 



TABLE I. 



SATURATED STEAM. 

ENGLISH UNITS. 



2 9 
p. 5b 

ifl 



32 
33 

34 
35 
36 

37 
38 
39 

40 

41 
42 
43 

44 
45 
46 

47 
48 
49 

50 

51 
52 
53 

54 
55 
56 

57 
58 
59 

60 



-Co 



0.0890 
0.0926 

0.0963 
0.1002 
0.1042 

0.1083 
0.1126 
0.1170 

0.1216 

0.1264 
0.1313 
0.1364 

0.1417 
0.1471 

0.1528 



0.1586 r.r. 

0.1646 "Z 
0.1708 % 



0.1773 

0.1839 

0.1908 
0.1979 

0.2052 
0.2128 
0.2206 

0.2287 
0.2370 
0.2456 



0.2545 



66 



61 0.2637 oA 

62 0.2731 il 

63 0.2829jQQ 




1.01 

2.01 
3.02 
4.03 

5.04 
6.04 
7.05 

8.06 

9.06 
10.07 
11.07 

12.08 
13.08 
14.09 

15.09 
16.10 
17.10 

18.10 

19.11 
20.11 
21.11 

22.11 
23.11 
24.11 

25.12 
26.12 
27.12 

28.12 

29.12 
30.12 
31.12 



1091.7 
1092.0 

1092.3 
1092.6 
1092.9 

1093.2 
1093.5 
1093.8 

1094.1 

1094.4 

1094.8 
1095.1 

1095.4 
1095.7 
1096.0 

1096.3 
1096.6 
1096.9 

1097.2 

1097.5 
1097.8 
1098.1 

1098.4 
1098.7 
1099.0 

1099.3 
1099.6 
1099.9 

1100.2 

1100.5 
1100.9 
1101.2 






1091.7 
1091.0 

1090.3 
1089.6 
1088.9 

1088.2 
1087.5 
1086.7 

1086.0 

1085.3 
1084.7 
1084.0 

1083.3 
1082.6 
1081.9 

1081.2 
1080.5 
1079.8 

1079.1 

1078.4 
1077.7 
1077.0 

1076.3 
1075.6 
1074.9 

1074.2 
1073.5 

1072.8 

1072.1 

1071.4 
1070.8 
1070.1 






1035.9 
1035.1 

1034.3 
1033.6 
1032.8 

1032.0 
1031.3 
1030.4 

1029.6 

1028.8 
1028.1 
1027.3 

1026.5 
1025.8 
1025.0 

1024.2 
1023.4 
1022.6 

1021.8 

1021.1 
1020.3 
1019.5 

1018.7 
1017.9 
1017.1 

1016.3 
1015.6 
1014.8 

1014.0 

1013.2 
1012.5 
1011.7 



•5« . 

Apu 



55.8 
55.9 

56.0 
56.0 
56.1 

56.2 
56.2 
56.3 

56.4 

56.5 
56.6 
56.7 

56.8 
56.8 
56.9 

57.0 
57.1 

57.2 

57.3 

57.3 
57.4 
57.5 

57.6 

57.7 
57.8 

57.9 
57.9 
58.0 

58.1 

58.2 
58.3 
58.4 



Oh^ 



rcdt 



0.0000 
0.0020 

0.0041 
0.0061 
0.0081 

0.0101 
0.0122 
0.0142 

0.0162 

0.0182 
0.0202 
0.0222 

0.0242 
0.0262 
0.0282 

0.0302 
0.0322 
0.0341 

0.0361 

0.0381 
0.0400 
0.0420 

0.0439 
0.0459 

0.0478 

0.0497 
0.0517 
0.0536 

0.0555 

0.0574 
0.0594 
0.0613 



3387 127 
3260 \g 



3138 
3022 
2910 

2803 
2700 
2601 

2506 



2415 

2328 
2244 

2164 

2087 
2013 

1942 

1874 



116 
112 
107 

103 
99 
95 

91 

87 
84 
80 

77 
74 
71 



1745 

1685 
1626 
1570 

1516 
1465 
1415 

1367 
1321 
1276 

1234 

1193 
1153 
1115 



Density, 



'S o c o 



0.0002952 
0.0003067 



115 
120 



0.0003187-,o9 

o.ooo3309|^;: 

0.0003436|3^ 

0.0003568. ofi 
0.0003704!^? 
0.0003845|^5 



0.0003990 

0.0004141 
0.0004296 
0.0004456 

0.0004621 
0.0004792 
0.0004968 

0.0005149 
0.0005336 
0.0005530, 

0.0005731 

0.0005937, 
0.0006150:.. Q 
0.0006369^20 

0.0006595oqj. 
0. 0006829^ J^ 
0.000706924g 

0.0007317^., 
0.00075715^0 
0.00078342^2 



151 



155 
160 
165 

171 
176 
181 

187 
194 
201 

206 

213 



0.0008104, 



280 



0.0008384 



0.0008673: 
0.0008969 



:;o289 



296 
304 






t 



32 
33 

34 
35 
36 

37 
38 
39 

40 

41 
42 

43 

44 
45 
46 

47 
48 
49 

50 

51 
52 
53 

54 
55 
56 

57 
58 
59 

60 

61 
62 
63 



SATURATED STEAM — Continued. 






64 
65 
66 

67 
68 
69 

70 

71 
72 
73 

74 
75 
76 

77 
78 
79 

80 

81 
82 
83 

84 
85 
86 

87 
88 
89 

90 

91 
92 
93 

94 
95 
96 

97 
98 
99 

100 

101 
102 
103 



0.2929 Q^ 
0.3033}^ 



0.3250 
0.3364 
0.3481 

0.3602 

0.3T26 
0.3854 
0.3986 



114 
117 
121 

124 

128 
132 
136 



0.4122... 
0.4202^"*" 



0.4406 



144 
149 



0.4555^ -q 
0.4708}'^^ 
0.4865}'^^ 



0.5027 



167 



0.5194.^1 
0.5365Ji^ 
0.5542}^} 

0.5723. Q- 
0.5910{^i 
0,6102}9^ 



203 
209 
214 



0.6299, 
0.6502; 
0.0711 

0.6925221 

^•2J!^226 
0. »3<22.3.. 

0.7605|:g 

0.7844.^,^ 
0.8090^-5 
0.8342-^ 

0.860l2.g 
0.8867o-q 
0.9140^^^ 

0.942Koo 



0.9709.^(,. 

1.00045^'5 
1.0307^3 



32.12 
33.12 
34.12 

35.12 
36.12 
37.12 

38.11 

39.11 
40.11 
41.11 

42.11 
43.11 
44.11 

45.10 
46.10 
47.09 

48.09 

49.08 
50.08 
51.07 

52.07 
53.06 
54.06 

55.05 
56.05 
57.04 

58.04 

59.03 
60.03 
61.03 

62.02 
63.02 
64.01 

65.01 
66.01 
67.01 

68.01 

69.01 
70.00 
71.00 



1101.5 
1101.8 
1102.1 

1102.4 
1102.7 
1103.0 

1103.3 

1103.6 
1103.9 
1104.2 

1104.5 
1104.8 
1105.1 

1105.4 
1105.7 
1106.0 

1106.3 

1106.6 
1107.0 
1107.3 

1107.6 
1107.9 
1108.2 

1108.5 
1108.8 
1109.1 

1109.4 

1109.7 
1110.0 
1110.3 

1110.6 
1110.9 
1111.2 

1111.5 
1111.8 
1112.1 

1112.4 






1069.4 
1068.7 
1068.0 

1067.3 
1066.6 
1065.9 

1065.2 

1064.5 
1063.8 
1063.1 

1062.4 
1061.7 
1061.0 

1060.3 
1059.6 
1058.9 

1058.2 

1057.5 
1056.9 
1056.2 

1055.5 
1054.8 
1054.1 

1053.4 
1052.7 
1052.1 

1051.4 

1050.7 
1050.0 
1049.3 

1048.6 
1047.9 
1047.2 

1046.5 
1045.8 
1045.1 

1044.4 



1112.7 1043. < 
1113.1 1043.1 
1113.4 ! 1042.4 



1010.9 
1010.1 
1009.4 

1008.6 
1007.8 
1007.0 

1006.2 

1005.4 
1004.6 
1003.8 

1003.0 
1002.3 
1001.5 

1000.7 
999.9 
999.1 

998.3 

997.5 
996.8 
996.0 

995.2 
994.4 
993.7 

992.9 
992.1 
991.4 

990.6 



989.0 
988.2 

987.4 
986.6 

985.8 

985.0 
984.2 
983.4 

982.7 

981.9 
981.2 
980.4 



Apu 



58.5 
58.6 
58.6 

58.7 
58.8 
58.9 

59.0 

59.1 
59.2 
59.3 

59.4 
59.4 
59.5 

59.6 
59.7 
59.8 

59.9 

60.0 
60.1 
60.2 

60.3 
60.4 
60.4 

60.5 
60.6 
60.7 

60.8 

60.9 
61.0 
61.1 

61.2 
61.3 
61.4 

61.5 
61.6 
61.7 

61.7 

61.8 
61.9 
62.0 



2 



■cdt 
T 



0.0632 
0.0651 
0.0670 

0.0689 
0.0708 
0.0727 

0.0745 

0.0764 
0.0783 
0.0802 

0.0820 
0.0839 
0.0858 

0.0876 
0.0895 
0.0913 

0.0932 

0.0950 

0.0968 
0.0987 

0.1005 
0.1023 
0.1041 

0.1060 
0.1078 
0.1096 

0.1114 

0.1132 
0.1150 
0.1168 

0.1186 
0.1204 
0.1222 

0.1240 
0.1258 
0.1275 

0.1293 

0.1311 
0.1329 
0.1347 



1042. 
1009 



107836 

33 

976.3.3.. 

044 / ^" 
914.32^0| 

885.0233 

856.7o-o 
829.5^^5 
803.2^1 



777.9 
753.5: 
729, 

707.1 
685.2 
664.1 



244 
236 

'228 

219 
211 

203 

197 

191 

184 
178 



568.8.^1 
o3o.2^gQ 



643.8 

624.1 
605.0 



519.2 
503.7 
488.9 

474.6 



155 
148 
143 

139 



460.' 



447.1 
434.0 



!l36 



131 
125 



421.5.^0 

409.3|f^ 
397.511^ 



386.1 
375.1 
364.4 

354.0. 



110 
107 
104 



344. lo(, 
334.5^^ 
325.2^^ 



Dexsity. 






0.0009273.31.3 
0.0009586q.r- 
0.0009911329 

0.001024.3- 
0.001059:3'? 
0.0010943g 

0.0011303^ 

0.001167qo 
0.001205^^ 
0.001245^j[ 

0.001286.. 
0.001327;.3 
0. 001370 J^ 

0.001414.. 
0.0014594g 



0.001505 
0.001553 



0.001602;=.. 
0.001653'?i 
0.0017055! 

0.001758.ri 
0.0018 1353 



0.001869 



57 



0. 001926;. q 

0.001985'^n 
0.002045g2 

0.002107^4 

0.002171aA 



0.002304 



0.002372^. 

002443I3 

0.002516-14 

0.002590^^ 
0.002666^^ 
0.002744gQ 

0.002824g2 

0.002906q. 
0.002990^^ 
0.003075^^ 



SATURATED STEAM — Continued. 



Bg 



5^ 



« " 1, 



-H5 



2 

'B 






Density. 






104 
105 
106 

107 
108 
109 

110 

111 
112 
113 

114 
115 
116 

117 
118 
119 

120 

121 
122 
123 

124 
125 
126 

127 
128 
129 

130 

131 
132 
133 

134 
135 
136 

137 
138 
139 

140 

141 
142 
143 



1.0619, 
1 



1.1266! 

1.1602, 
1.194T 
1.2301 



319 

328 
336 



1.2663 



345 
354 

362 

372 



1.3035OQ-, 
1.3416gJ 



1.4207 
1.4618* 
1.5039 

1.5470 
1.5912 
1.6364" 



411 
421 
431 

442 
452 
464 



1.6828^^4 

1.7302,;.- 
1.7789!^i 



1.8287 



510 



1.8797-21 
1.9318'^^i 
1.9852^^^ 

2.0399-«^ 
2.0959'5^0 

2.1533^?^4 



2.2119 



600 



2.2719 
2.3333 
2.3961 

2.4603 
2.5261 
2.5932; 

2.6619 
2.7321 
2.8040, 



614 

628 
642 



,671 
687 



702 
719 
734 



2.8774,5, 

2..9o257«7 
3.0292ir 



3.1076 



784 
801 



72.0 
73.0 
74.0 

75.0 
76.0 
77.0 

78.0 

79.0 
80.0 
81.0 

82.0 
83.0 
84.0 

85.0 
86.0 
87.0 

88.1 

89.1 
90.1 
91.1 

92.1 
93.1 
94.1 

95.1 
96.1 
97.1 

98.1 

99.1 

100.2 

101.2 

102.2 
103.2 
104.2 

105.2 
106.2 
107.2 

108.2 

109.2 
110.2 
111.2 



1113.7 
1114.0 
1114.3 

1114.6 
1114.9 
1115.2 

1115.5 

1115.8 
1116.1 
1116.4 

1116.7 
1117.0 
1117.3 

1117.6 
1117.9 
1118.2 

1118.5 

1118.8 
1119.2 
1119.5 

1119.8 
1120.1 
1120.4 

1120.7 
1121.0 
1121.3 

1121.6 

1121.9 
1122.2 
1122.5 

1122.8 
1123.1 
1123.4 

1123.7 
1124.0 
1124.3 

1124.6 

1124.9 
1125.3 
1125.6 



1041.7 
1041.0 
1040.3 

1039.6 
1038.9 
1038.2 

1037.5 

1036.8 
1036.1 
1035.4 

1034.7 
1034.0 
1033.3 

1032.6 
1031.9 
1031.2 

1030.4 

1029.7 
1029.1 
1028.4 

1027.7 
1027.0 
1026.3 

1025.6 
1024.9 
1024.2 

1023.5 

1022.8 
1022.0 
1021.3 

1020.6 
1019.9 
1019.2 

1018.5 
1017.8 
1017.1 

1016.4 

1015.7 
1015.1 
1014.4 



979.6 

978.8 
978.0 

977.2 
976.4 
975.6 

974.8 

974.0 
973.2 
972.4 

971.6 

970.8 
970.0 

969.2 
968.4 
967.6 

966.7 

966.0 
965.3 
964.5 

963.7 

962.9 
962.1 

961.3 
960.5 
959.7 

958.9 

958.1 
957.2 
956.4 

955.6 
954.8 
954.0 

953.2 
952.4 
951.6 

950.8 

950.0 
949.3 
948.5 



62.1 
62.2 
62.3 

62.4 
62.5 
62.6 

62.7 

62.8 
62.9 
63.0 

63.1 
63.2 
63.3 

63.4 
63.5 
63.6 

63.7 

63.7 

63.8 
63.9 

64.0 
64.1 
64.2 

64.3 
64.4 
64.5 

64.6 

64.7 
64.8 
64.9 

65.0 
65.1 
65.2 

65.3 
65.4 
65.5 

65.6 

65.7 
65.8 
65.9 



0.1364 
0.1382 
0.1400 

0.1417 
0.1435 
0.1452 

0.1470 

0.1487 
0.1505 
0.1522 

0.1540 

0.1558 
0.1575 

0.1592 
0.1610 
0.1627 

0.1645 

0.1662 
0.1679 
0.1697 

0.1714 
0.1731 
0.1748 

0.1765 
0.1783 
0.1800 

0.1817 

0.1834 
0.1851 
0.1868 

0.1885 
0.1902 
0.1919 

0.1936 
0.1952 
0.1969 

0.1986 

0.2003 
0.2020 
0.2036 



316.1qq 

307.3^? 
298.8| 

290.6-Q 

282.7^:; 
275.0{^ 

267.5,2 

260 3.^ 
253.3'^ 
246.5^^ 

239.9^4 
233.5^1 
227.3^2 

221.3^0 
215.5;5« 
209.9^« 

204.4-3 

199.1-2 
193.9?^ 

188.9^^ 



184.1 
179.4 
174 

170.4 
166.1 
161.! 

157.8c 

153.9, 
150.1 
146.4; 

142.8 
139.2 
135.8 

132.5 



129.3: 
126.2; 

123.2 



120.200 
117.3| 
114.5^:^ 



0.003163o. 
0.003254^.^ 
0.003347g^ 



0.003441 
0.003537 
0.003636 

0.003738 



96 
99 
102 



104 
0.003842 ()g 

0.003948{^o 
0.004057{j'5^ 



0.004168 
0.004283 
0.004399 

0.004519 
0.004640 
0.004764 

0.004892 



115 
116 
120 

121 

124 
128 

130 



0.005022-10. 

0.005156;q7 

0.005293!oa 
lo\) 



0.005432 
0.005574 
0.005720: 



142 
146 
148 



0.005868.^9 
0. 006020} '?f 
0.006176^^^ 



0.006336 

0.006498 
0.006664 
0.00683^ 



162 

166 
169 
172 



0.007005. ^« 
0.00718lj'^ 
0.00736l|g^ 



0.007545 
0.007732 
0.007924 

0.008120 



187 
192 
196 



198 



0.008318.^^, 
0.008522!;^ J 
0.0087302]^^ 



104 
105 
106 

107 
108 
109 

110 

111 
112 
113 

114 
115 
116 

117 
118 
119 

120 

121 
122 
123 

124 
125 
126 

127 
128 
129 

130 

131 
132 
133 

134 
135 
136 

137 
138 
139 

140 

141 
142 
143 



SATURATED BT BAM— Continued. 






144 
145 
146 

147 
148 
149 

150 

151 
152 
153 

154 
155 
156 

157 
158 
159 

160 

161 
162 
163 

164 
165 
166 

167 
168 
169 

170 

171 
172 
173 

174 
175 
176 

177 
178 
179 

180 

181 
182 
183 






3. 1877;.. q 
3.2696^.^^ 
3.3532|^ 

3.4387.^. 



3.6152; 
3.7063, 



911 



930 

3.7993 5 

3.8943j^^ 

3.9913ygQ 

4.0903.Q.. 
4.1914|^.ll 

^•^^^^1054 

4.4000,,,^- 
4.50(0 Qq- 
4 617'> 



4.7292 



4.8435 
4.9601 



5.079 

5.200 
5.324 
5.450 

5.579 
5.710 
5.844 

5.981 



1143 

1166 
1189 



121 



124 
126 
129 

131 
134 
137 

139 



6.120^42 
6.26?^ - 



6.407 



145 
147 



6.554 .. 
6.704^^ 
6.858}^^ 

'•^.'ei62 

7.500^g3 

7.668.2 
7.840;Ij 
8.014}:^ 



112.2 
113.3 
114.3 

115.3 
116.3 
117.3 

118.3 

119.3 
120.3 
121.3 

122.3 
123.3 
124.3 

125.4 
126.4 
127.4 

128.4 

129.4 
130.4 
131.4 

132.4 
133.4 
134.4 

135.4 
136.4 
137.4 

138.5 

139.5 
140.5 
141.5 

142.5 
143.5 
144.5 

145.5 
146.5 
147.5 

148.5 

149.5 
150.6 
151.6 



1125.9 
1126.2 
1126.5 

1126.8 
1127.1 
1127.4 

1127.7 

1128.0 
1128.3 
1128.6 

1128.9 
1129.2 
1129.5 

1129.8 
1130.1 
1130.4 

1130.7 

1131.0 
1131.4 
1131.7 

1132.0 
1132.3 
1132.6 

1132.9 
1133.2 
1133.5 

1133.8 

1134.1 
1134.4 
1134.7 

1135.0 
1135.3 
1135.6 

1135.9 
1136.2 
1136.5 

1136.8 

1137.1 
1137.5 
1137.8 



^> 



1013.7 
1012.9 
1012.2 

1011.5 
1010.8 
1010.1 

1009.4 

1008.7 
1008.0 
1007.3 

1006.6 
1005.9 
1005.2 

1004.4 
1003.7 
1003.0 

1002.3 



1001.6 934.0 
1001.0 933.3 
1000.3 932.5 



947.7 
946.8 
946.0 

945.2 
944.4 
943.6 

942.8 

942.0 
941.3 
940.5 

939.7 
938.9 
938.1 

937.2 
936.4 
935.6 

934.8 



999.6 
998.9 
998.2 

997.5 
996.8 
996.1 

995.3 

994.6 
993.9 
993.2 

992.5 
991.8 
991.1 

990.4 
989.7 
989.0 



931.7 
930.9 
930.1 

929.3 

928.5 
927.7 

926.8 

926.0 
925.2 
924.4 

923.7 
922.9 
922.1 

921.3 
920.5 
919.7 

918.9 



987.6 918.1 
986.9 ' 917.3 
986.2 I 916.5 






A/u 



66.0 
66.1 
66.2 

66.3 
66.4 
66.5 



66.7 
66.7 
66.8 



67.0 
67.1 

67.2 
67.3 
67.4 

67.5 

67.6 
67.7 
67.8 

67.9 
68.0 
68.1 

68.2 
68.3 
68.4 

68.5 

68.6 
68.7 



68.9 
69.0 

69.1 
69.2 
69.3 

69.4 

69.5 
69.6 
69.7 






■rcdt 
J T 



0.20,53 
0.2070 
0.2086 

0.2103 
0.2119 
0.2136 

0.2152 

0.2169 
0.2185 
0.2202 

0.2218 
0.2235 
0.2251 

0.2267 
0.2284 
0.2300 

0.2316 

0.2332 
0.2349 
0.2365 

0.2.381 
0.2307 
0.2413 

0.2429 
0.2445 
0.2461 

0.2477 

0.2493 
0.2509 
0.2525 

0.2541 
0.2557 
9.2573 

0.2589 
0.2604 
0.2620 

0.2636 

0.2652 
0.2667 
0.2683 



111.826 
109.2^^ 
IO6.625 



104.1 
101.7 
99.33: 

97.03 



24 
24 



94.79 
92.61 
90.49; 



230 

224 

218 
212 
206 



88.4.3 

86.42201 

84.471^0 



82.56 
80.70 
78.90 

77.14 

75.43 
73.77 
72.14 



186 
180 
176 



171 



106 
163 
158 



70.56... 

69.01 ^2 
67.51]^^ 



66.05 
64.62 
63.22 

61.85 



143 
140 
137 

132 



60.53. oQ 
59.25}| 
57.99j^^ 



56.76 
55.56 
54.40 

53.26 
52.14: 
51.06: 

50.01 



48.98 
47.9 



46.99; 



120 
116 
114 

112 
108 
105 

103 

101 

'98 



96 



Density. 



« o = o 



0.008942^-, w 
0.009159-:^/. 
0.009379225 

0.009604220 
0.009833^07 
0.010072^^ 



0.01031 



24 



0.01055.,- 
0.01080n? 
0.011052g 

0.01131.-.« 
0.01157;H 
0.011842Y 

0.01211^0 
0.0123955 
0.0120729 

O.OI2963Q 

0.01326oA 
0.01356:^" 
9.0138635* 



0.01417 
0.01449' 
0.01481' 



0.01514o. 
0.01548ot 
0.01582g 

O.OI6I735 

0.01652 



0.01688c 



36 



36 



0.017241 

0.01762qQ 

0.0180000 

0.01838|g 
0.01878,r^ 



0.01918 
0.01958' 



O.O2OOO42 

0. 02042. o 
0.02085 J3 



0.02128 



'44 



SATURATED STB AM— Continued. 



I'i 


;: O y 


3 

A 


1 


H 


1 


1- 


ll 


2 


a 

3 

I 

•3 


Density. 


it 

P 


« c 


^ 


P 


Q 


A 


r 


p 


Apu 


rcdt 
J T 


J 


Y 


t 


184 
185 
186 


8.192. Q. 

8.558|| 


1.52.6 
153.6 
154.6 


1138.1 
1138.4 
1138.7 


985.5 

984.8 
984.1 


915.7 
914.9 
914.1 


69.8 
69.9 
70.0 


0.2699 
0.2714 
0.2730 


46.03^4 
45.09^1 
44.17^2 


0.02172.« 
0.02218^^ 
0.02264J^ 


184 
185 
186 


187 
188 
189 


8.937}^i 
9.132|^g 


1.55.6 
1.06.6 
157.6 


1139.0 
1139.3 
1139.6 


983.4 

982.7 
982.0 


913.4 
912.6 
901.8 


70.0 
70.1 
70.2 


0.2745 
0.2761 
0.2777 


43.28^7 
42.41^^ 
41.56|^ 


0.02311,7 
0. 02358 Ji 
0.024064^ 


187 
188 
189 


190 


9.330^02 


158.6 


1139.9 


981.3 


911.0 


70.3 


0.2792 


40.73gi 


0.02455.0 


190 


191 
192 
193 




159.6 
160.6 
161.6 


1140.2 
1140.5 
1140.8 


980.6 
979.9 
979.2 


910.2 
909.4 
908.6 


70.4 
70.5 
70.6 


0.2808 
0.2823 
0.2838 


39.92^0 
39.134^ 
38.35^« 


0.02505... 
0.025569:^ 
0.02608^^ 


191 
192 
193 


194 
195 
196 


10.160.-,^ 
ia3772^{ 
10.598^^^ 


162.6 

163.7 
164.7 


1141.1 
1141.4 
1141.7 


978.5 
977.7 
977.0 


907.8 
906.9 
906.2 


70.7 
70.8 
70.8 


0.2854 
0.2869 

0.2885 


37.597, 
36.85'^ 
36.13^^ 


0.02660., 
0.02714^* 
0. 02768^1 


194 
195 
196 


197 
198 
199 


11.051^^.^ 
11-2832^7 


165.7 
166.7 
167.7 


1142.0 
1142.3 
1142.6 


976.3 
975.6 
974.9 


905.4 
904.6 
908.8 


70.9 
71.0 
71.1 


0.2900 
0.2915 
0.2930 


34:73^^ 
34.06^^ 


02823.^ 
0.02879?? 
0.02936^^ 


197 
198 
199 


200 


11.520241 


168.7 


1142.9 


974.2 


903.0 


71.2 


0.2946 


33.40g4 


0.02994.g 


200 


201 
202 
203 


11.761244 
12.254-^9 


169.7 
170.7 
171.7 


114.3.2 
1143.6 
1143.9 


973.5 
972.9 
972.2 


902.2 
901.5 
900.8 


71.3 
71.4 

71.4 


0.2961 
0.2976 
0.2991 


32.76«o 
32.13^^1 
31.52^J 


0.03053.Q 
0.03112^? 
0.03173^^ 


201 
202 
203 


204 
205 
206 


12..508..^7 
12.765^«' 
13.0282^^ 


172.7 
173.7 
174.7 


1144.2 
1144.5 
1144.8 


971.5 
970.8 
970.1 


900.0 

899.2 
898.4 


71.5 

71.6 

71.7 


0.3007 
0.3022 
0.3037 


30.9250 
30.33?; 
29.76^j 


0.03235^^ 
0.03297^^ 
0.03361^9 


204 
205 
206 


207 
208 
209 


13.294^7. 
13..565^1« 
13.8415^J 


175.8 

176.8 
177.8 


1145.1 
1145.4 
1145.7 


969.3 
968.6 
967.9 


897.5 
896.7 
896.0 


71.8 
71.9 
71.9 


0..3052 
0.3067 
0.3082 


29.19.^ 
28.639V 
28.09g 


0.03426.- 
0.03493X7 
0.03560^^ 


207 
208 
209 


210 


14.122285 


178.8 


1146.0 


967.2 


895.2 


72.0 


0.3097 


27.57^2 


0.03628gg 


210 


211 
212 
213 


14:697^^^ 
14.990|3 


179.8 
180.8 
181.8 


1146.3 
1146.6 
1146.9 


966.5 
965.8 
965.1 


894.4 
893.5 
892.6 


72.1 
72.3 
72.5 


0.3112 
0.3127 
0.3142 


27.0545 
26. 60S 
26.16|^ 


0.03697.O 

0.03760^2 
0.03824^1 


211 
212 
213 


214 
215 
216 


15.289303 
15.592!^^^ 
15.901^J| 


182.8 
183.8 
184.8 


1147.2 
1147.5 
1147.8 


964.4 
963.7 
963.0 


891.8 
891.0 
890.2 


72.6 

72.7 
72.8 


0.3157 

0.3172 
0.3187 


25.67_^ 
25.19TX 
24.73^^ 


0.03896^0 
0.03969^? 
0.04043^5 


214 
215 
216 


217 
218 
219 


16.214..-, Q 
16.533^^ 
16.857|^ 


185.8 

186.8 
187.8 


1148.1 
1148.4 
1148.7 


962.3 
961.6 
960.9 


889.5 

888.7 
887.9 


72.8 
72.9 
73.0 


0.3202 
0..3217 
0.3232 


24.2844 
23.84|t 
23.41^ 


0.04118^^ 
0.04194ix 
0.04272^5 


217 
218 
219 


220 


I7.I86335 


188.9 


1149.0 


960.1 


887.1 


73.0. 


0.3246 


22.9842 


0.04352gQ 


220 


221 
222 
223 


17 Gdlg^ 
18.206|J 


189.9 
190.9 
191.9 


1149.3 
1149.7 
1150.0 


959.4 
958 8 
958.1 


886.3 
885.6 

884.8 


7.3.1 
73.2 
73.3 


0.3261 
0..3276 
0.3291 


22.564. 


0.04432qo 
0.04514^^ 
0.04596^4 


221 
222 
223 



SATURATED STEAM— Continued. 



Z.il> 



224 
225 
226 

227 
228 
229 

230 

231 
232 
233 

234 
225 
236 

237 
238 
239 

240 

241 
242 
243 

244 
245 
246 

247 
248 
249 

250 

251 
252 
253 

254 
255 
256 

257 
258 
259 

260 

261 
262 
263 



18.557, 



18.914;: 



357 



19.276|| 

20. 01 807 J 
20.397g^ 

20.783392 

21.175oQ7 
21.572'^"! 



404 
410 

417 
423 
429 

436 
442 
449 

456 

462 

26.846^3^ 
27.330^^^ 
27.82Cno 



21.976_ 

22. .386 
22.80: 
23.220 

23.655 
24.091 
24.533 

24.982 

25.438 



28.319, 

28.824; 
29.336] 

29.856, 

30.384 
30.919; 
31.462 



505 
512 
520 

528 

535 
543 
550 



32.012..Q 
32.67r?2^ 
33.1375^^ 

33.711.^0 
34.294^^^ 
34.884gg9 



35.483, 

36.090, 
36.706 
37.330, 



607 

'616 
624 
633 



192.9 
193.9 
194.9 

195.9 
196.9 
197.9 

198.9 

199.9 
201.0 
202.0 

203.0 
204.0 
205.0 

206.0 
207.0 
208.0 

209.0 

210.0 
211.0 
212.0 

213.0 
214.1 
215.1 

216.1 
217.1 
218.1 

219.1 

220.1 
221.1 
222.1 

223.1 
224.1 
225.1 

226.2 

227.2 
228.2 

229.2 

230.2 
231.2 
232.2 



1150.3 
1150.6 
1150.9 

1151.2 
1151.5 
1151.8 

1152.1 

11.52.4 
1152.7 
1153.0 

1153.3 
1153.6 
1153.9 

1154.2 
1154.5 
1154.8 

1155.1 

1155.4 
1155.8 
1156.1 

1156.4 
1156.7 
1157.0 

1157.3 
1157.6 
1157.9 

1158.2 

1158.5 
1158.8 
1159.1 

1159.4 

1159.7 
1160.0 

1160.3 
1160.6 
1160.9 

1161.2 

1161.5 
1161.9 
1162.2 



o a, 



957.4 
956.7 
956.0 

955.3 
954.6 
953.9 

953.2 

952.5 
951.7 
951.0 

950.3 
949.6 
948.9 

948.2 
947.5 
946.8 

946.1 

945.4 
944.8 
944.1 

943.4 
942.6 
941.9 

941.2 
940.5 
939.8 

939.1 

938.4 
937.7 
937.0 

936.3 
935.6 
934.9 

934.1 
933.4 
932.7 

932.0 

931.3 
930.7 
930.0 



884.0 
883.3 
882.5 

881.7 
880.9 
880.2 

879.4 

878.6 
877.8 
877.0 

876.2 
875.4 
874.6 

873.9 
873.1 
872.3 

871.6 

870.8 
870.1 
869.3 

868.5 
867.7 
866.9 

866.1 
865.3 
864.5 

863.8 

863.0 
862.2 
861.4 

860.7 
859.9 
859.1 

858.2 
857.5 
856.7 

855.9 

855.1 
854.4 
853.7 






A/7i 



73.4 
73.4 
73.5 

73.6 
73.7 
73.7 

73.8 

73.9 
73.9 
74.0 

74.1 
74.2 
74.3 

74.3 
74.4 
74.5 

74.5 

74.6 
74.7 
74.8 

74.9 
74.9 
75.0 

75.1 
75.2 
75.3 

75.3 

75.4 
75.5 
75.6 

75.6 
75.7 
75.8 

75.9 
75.9 
76.0 

76.1 

76.2 
76.3 
76.3 






0..3305 
0..3320 
0.3335 

0.3349 
0.3364 
0.3379 

0.3393 

0.3408 
0.3423 
0.3437 

0.3452 
0.3466 
0.3481 

0.3495 
0.3510 
0.3524 

0.3538 

0.3.553 
0.3567 
0.3581 

0.3596 
0.3610 
0.3624 

0.3639 
0.3653 
0.3667 

0.3681 

0.3695 
0.3709 
0.3724 

0.3738 
0.3752 
0.3766 

0.3780 
0.3794 
0.3808 

0.3822 

0.3836 
0.3850 
0.3864 



21..37oQ 
20.99"^? 
20.62:^4 

u t 

20.25o. 
19.89;::? 
19.54-^ 

^3 



19.20 



IS. 87.3.3 
18.54;J^ 

18.22^2 



17.90 
17.59 
17.29; 

16.99, 
16.70; 
16.42; 

16.14, 



15.87.7 
15.60;^ 
15.34|^ 

15.08.2. 

14.58^^ 



14..34, 
14.11 

13.88: 

13.65, 

13.43 

13.21 
12.99; 



12.7821 
12.57|J 
12.37|^ 



12.17 
11.98 
11.79 

11.60 

11.42 
11.24 
11.06 



Density. 



0.04679q^ 
0.04764^^ 
0.04850^0 



0.04938, 
0.05028; 
0.05118, 

0.05208 



O.O53OO01 
0.65304^3 
0.05489^^ 

0.05586oQ 
0.05685^^ 
0.05784J^j 



0.05885 
0.05987 
0.06090 

0.06195 

0.06301 
0.06409 
0.06519 



102 
103 
105 

106 

108 

no 
111 



0.06630,10 244 
0.06743|!'' 245 
0.06858{J? 

0. 06973,. p^ 
0. 07089.^ ^'^ 



118 
120 



0.07207 

0.07327^21 

0.07448, oQ 
^07571 1'^ 



0.07( 



0.07825 
0.07953 
0.08082 

0.08214 
0.08347 
0.08482 

0.08619 



128 
129 
132 

133 
135 
137 

138 



0.08757 



0.0889' 



'140 



0.09039 



(142 



143 



254 
255 
256 

257 
258 
259 

260 

261 
262 
263 



SATURATED STU A.M— Continued. 



CutD 

i 



264 
265 
266 

267 
268 
269 

270 

271 
272 
273 

274 
275 
276 

277 
278 
279 

280 

281 
282 
283 

284 
285 
286 

287 
288 
289 

290 

291 
292 
293 

294 
295 
296 

297 
298 
299 

300 

301 
302 
303 






37.963, 

38.604 
39.255; 

39.914 

40.582 
41.259, 

41.945, 



641 
651 
659 

;668 
677 
686 

695 



44.059^14 



44.782, 



45.515 



733 



.o743 



46.258^53 

47.011-^^,^ 

47.773 '7; 



49.328, 

50.12.^ 

50.92^^ 
51.74| 

52.56qo 
53.39°e 



792 



85 



54.24 



55.09o7 
55.96^1 
56.83o^ 



57.72, 

58.62, 
59.53, 
60.45, 



61.38.. 
62.33;^? 

63.28^^ 

6o.23qq 
66.22 



67.22 

68.24 
69.27 
70.30 



lOO 

102 

103 
103 
106 



233.2 
234.2 
235.2 

236.2 

2.37.2 

238.2 

239.3 

240.3 
241.3 
242.3 

243.3 
244.3 
245.3 

246.3 

247,3 
248.3 

249.3 

2.50.3 
251.4 
252.4 

2.53.4 
254.4 
255.4 

256.4 

257.4 
258.4 

259.4 

260.4 
201.4 
262.4 

263.4 
264.5 
265.5 

266.5 
267.5 

268.5 

269.5 

27(^.5 
271.5 

272.5 



1162.5 
1162.8 
1163.1 

1163.4 
1163.7 
1164.0 

1164.3 

1164.6 
1164.9 
1165.2 

1165.5 
1165.8 
1166.1 

1166.4 
1166.7 
1167.0 

1167.3 

1167.6 
1168.0 
1108.3 

1168.6 
1168.9 
1169.2 

1169.5 
1169.8 
1170.1 

1170.4 

1170.7 
1171.0 
1171.3 

1171.6 
1171.9 
1172.2 

1172.5 
1172.8 
1173.1 

1173.4 

1173.7 
1174.1 
1174.4 






929.3 
928.6 
927.9 

927.2 
926.5 

92.5.8 

925.0 

924.3 
923.6 

922.9 

922.2 
921.5 
920.8 

920.1 
919.4 
918.7 

918.0 

917.3 
916.6 
915.9 

915.2 
914.5 
913.8 

913.1 
912.4 
911.7 

911.0 

910.3 
909.6 
908.9 

908.2 
907.4 
906.7 

906.0 
905.3 
904.6 

903.9 

903.2 
902.6 
901.9 



<u Or*- 
P 



852.9 
852.1 
851.3 

850.6 
849.8 
849.0 

848.1 

847.4 
846.6 
845.8 

845.0 
844.2 
843.5 

842.7 
841.9 
841.1 

840.4 

839.6 

838.8 
838.0 

837.2 
836.5 
835.7 

834.9 
834.1 
833.4 

832.6 

831.8 
831.0 
830.3 

829.5 

828.6 
827.8 

827.0 
826.3 
825.5 

824.7 

823.9 
823.3 
822.5 



Apic 



76.4 
76.5 
76.6 

76.6 
76.7 
76.8 

76.9 

76.9 
77.0 
77.1 

77.2 
77.3 
77.3 

77.4 
77.5 
77.6 

77.6 

77.7 
77.8 
77.9 

78.0 

78.0 
78.1 

78.2 
78.3 
78.3 

78.4 

78.5 
78.6 
78,6 

78.7 
78.8 
78.9 

79.0 
79.0 
79.1 

79.2 

79.3 
79.3 
79.4 



IM 



'[cdt 
J T 



0.3878 
0.3891 
0.3906 

0.3919 
0.3933 
0.3947 

0.3961 

0.3975 
0.3988 
0.4002 

0.4016 
0.4030 
0.4043 

0.4057 
0.4071 
0.4084 

0.4098 

0.4112 
0,4125 
0.4139 

0.4152 
0.4166 
0.4179 

0.4193 
0.4206 

0.4220 

0.4233 

0.4247 
0.4200 
0.4273 

.0.4287 
0.4300 
0.4313 

0.4327 
0.4340 
0.4353 

0.4366 

0.4.380 
0.4393 
0.4406 



10.89 
10.72 
10.55 

10.39 
10.23 
10.07 



15 



9.918 

9.766 
9.617 
9.471 

9.328 
9.187 
9.049 



152 



149 
146 
143 

141 
138 
136 



8.91.3.00 
8.780|?? 
8.649}^^ 



8.521 

8.395 
8.271 
8.149 



126 

124 

122 
119 



8.030. -,« 
7.913}^^ 
7.797}1J 

7.573-. ^q 
7.464{0^ 

7.356^05 



7.251 
7.148 
7.046 

6.946, 
6.847 
6.750; 



103 
102 
100 

'99 

'SI 

95 



6.655oq 
6.562^5 
6.470^5 



5.380, 



6.292 
6.205! 
6.119: 



Density. 



0.09182 

0.09327 
0.09474 



145 
147 
150 



0.09624..-, 
0.09775!^^ 
0.09927iro 

0.1008-^g 

0.1024.^ 
0.1040!^ 
0.1056Jg 



0.1072 
0.1088 
0.1105 

0.1122 
0.1139 
0.1156 

0.1173 

0.1191 
0.1209 
0.1227 

0.1245 
0.1264 
0.1283 

0.1302 
0.1321 
0.1340 

0.1359, 



20 



0.1379, 



0.1399; 
0.1419; 

0.1440, 
0.1461 
0.1482; 



0.1503^-, 
0.1524;} 
0.1545-2 



0.1567 

0.1589, 
0.1611 
0.1634 



264 
265 
266 

267 
268 
269 

270 

271 
272 
273 

274 
275 
276 

277 
278 
279 

280 

281 
282 
283 

284 
285 
286 

287 

288 
289 

290 

291 
292 
293 

294 
295 
296 

297 
298 
299 

300 

301 
302 
303 



SATURATED STU AM — Continued. 






304 
305 
003 

307 
303 
309 

310 

311 
312 
313 

314 
315 
316 

317 
318 
319 

320 

321 
322 
323 

324 
325 
326 

327 
328 
329 

330 

331 
332 
333 

334 
335 
336 

337 
338 
339 

340 

341 
342 
343 






.4. 59 
(G.SO 
rT.93 



110 
111 
113 

114 



79.07. i« 

t,r> f,ollO 



81.39 



118 



84.98{21 

8--??123 

88.68}^^ 

89.95j^g 
92.525^ 



95.14 

9(3.48 
97.83 



134 
135 
137 



99.20. 00 

101.97J^J 

103.38^43 

104.81... 
10(i.2oJ^| 
107.70|J^ 

109.17.40 

1 10.66 JtV 
112.17}?! 

113.69. -o 
115.22{g 
II6.77}- 



118.34 



159 



119.93.^^ 
121.53^0 

123.15}^2 



273.0 1174.7 
274.5 1175.0 

275.5 I 1175.3 

276.6 ! 1175.6 
277.6 : 1175.9 
278.6 1176.2 

279.6 1176.5 



280.6 
281.6 
282.7 



290.0 

291.0 
292.1 
293.1 

294.2 
295.2 
296.3 

297.3 
298.4 
299.4 

300.5 

301.5 
302.6 
303.6 

304.6 

305.7 
306.7 

307.8 
308.8 
309.9 

310.9 

312.0 
313.0 
314.1 



1176.8 
1177.1 
1177.4 



283.7 1177.7 

284.8 1178.0 

285.8 1178.3 

286.9 1178.6 
2S7.9 1178.9 
289.0 1179.2 



1179.5 

1179.8 

1180.2 
1180.5 

1180.8 
1181.1 
1181.4 

1181.7 
1182.0 
1182.3 

1182.6 

1182.9 
1183.2 
1183.5 

1183.8 
1184.1 
1184.4 

1184.7 
1185.0 
1185.3 

1185.6 

1185.9 
1186.3 
1186.6 



901.2 
900.5 
899.8 

899.0 
898.3 
897.6 

896.9 

896.2 
895.5 
894.7 

894.0 
893.2 
892.5 

891.7 

801.0 
890.2 

880.5 

888.8 

8S8.1 
887.4 

886.6 
885.9 
885. 1 

884.4 
883.6 
882.9 

882.1 

881.4 
880.6 
879.9 

879.2 

878.4 

877.7 

876.9 
876.2 
875.4 

874.7 

873.9 
873.3 
872.5 



p 



821.7 
820.9 
820.1 

819.3 

818.5 
817.7 

817.0 

816.2 
815.4 
814.5 

813.8 
812.9 
812.1 

811.3 

810.5 
809.6 



808.1 
807.3 
806.5 

805.7 
804.9 
804.1 

803.3 
802.4 
801.6 

800.8 

800.0 
799.1 
7 



5.4 



797.6 

796.7 
796.0 

795.1 
794.3 
793.5 

792.7 



-S3 



79.5 
79.6 
79.7 

79.7 

79.8 
79.9 

79.9 

80.0 
80.1 
80.2 

80.2 
80.3 
80.4 

80.4 
80.5 
80.6 

80.74 

80.7 
80.8 
80.9 

80.9 
81.0 
81.1 

81.1 
81.2 
81.3 

81.3 

81.4 
81.5 
81.5 

81.6 
81.7 
S1.7 

81.8 
81.9 
81.9 

82.0 



791.8 82.1 

791.2 I 82.1 

790.3 ' 82.2 



8 



I- 

tcdt 
J T 



0.4419 
0.4433 
0.4446 

0.4459 
0.4472 
0.4485 

0.4498 

0.4511 
0.4524 
0.4538 

0.4552 
0.4565 
0.4579 

0.4592 
0.46C6 
0.4619 

0.4633 

0.4646 
0.4659 
0.4672 

0.4686 
0.4699 
0.4713 

0.4726 
0.4739 
0.4752 

0.4766 

0.4779 
0.4792 
0.4805 

0.4818 
0.4832 
0.4845 

0.4a58 
0.4871 
0.4884 

0.4897 

0.4910 
0.4923 
0.4936 



6.035qo 
5.952^? 
5.871^J 

5.791-c) 
5.7121^ 
5.634*^ 

5.558«- 

5.4844 
5.410I0 
5.337^'^ 

5.266.,-, 



5.195, 
5.126 



5.058^- 



4.991 
4.925; 

4.861, 



1:^73- 

4.493?? 

4.436.^ 
4.379?^ 
4.323?^ 

4.26754 

4.21354 
4.159'?o 
4.107| 

4.055.. 
4.004^J 
3.954?^ 

3.90440 
3.855|^ 
3.807|° 

3.7604^ 

3.71345 
3.6681? 
8.62343 



Density. 



o o - o 
^2h oE=, 



0.16.57, 
O.I68O; 
0.1703; 



0.1727^4 
0.1751^1 
0.1775^J 



o.r 



'24 



O.I8235. 
0.1848^'? 
0.1873^3 

1899^. 
0.192.5;^ 
0.1951|^ 



0.1977, 
0.2004; 
0.2031 



27 



0.2058- 



27 



0.2085. 



0.2112 
0.2140 



0.2168.O 
0.2197^^ 
0.2226^Q 



0.2255 

0.2284; 
0.2313 



30 
0.234331 

0.2374on 
0.2404'^y 

0.2435:^1 

0.2466on 
0.2498of 
0.2529g 

0.2561oQ 
0.2594'^:^ 
0.2627-^ 

O.266O33 

0.26Q3oq 
0.2726o2 
0.2760o- 



SATURATED STU A. M — Continued. 



1- 

i 


'I 

m . 

ill 

I 1 


,3 

i 



1 


1 


1 
1 

r 


> s 


I1; 




3 
"o 
!> 

1 


Density. 




•Sol 


^ 


/ 


9 


A. 


r 


p 


Apu 


[cat 
J T 


s 


^ 


t 


344 
345 
346 


12478... 
128.10}^^ 


315.1 
316.1 
317.2 


1186.9 
1187.2 
1187.5 


871.8 
871.1 
870.3 


789.5 
788.8 
787.9 


82.3 
82.3 

82.4 


0.4949 
0.4962 
0.4975 


3.578_^4 
3.534 ,f^ 
3.49lg 


0.2795..^ 
0.2830g 
0.2865g 


344 
345 
346 


347 
348 
349 


131.49tIo 
133.21}?^ 


318.2 
319.3 
320.3 


1187.8 
1188.1 
1188.4 


869.6 

868.8 
868.1 


787.1 
786.3 

785.5 


82.5 
82.5 
82.6 


0.4988 
0.5001 
0.5014 


3.449, 
3.407J; 
3.365 J^ 


O.29OO0K 
0.2935o^ 
0.2971^^ 


347 
348 
349 


350 


134.95^^3 


321.4 


1188.7 


867.3 


784.7 


82.6 


0.5027 


3.3244() 


0.30083^ 


350 


351 
352 
353 


138.48}{^ 
140.27}^^ 


322.4 
323.5 
324.5 


1189.0 
1189.3 
1189.6 


866.6 
865.8 
865.1 


783.9 
783.0 
782.3 


82.7 
82.8 
82.8 


0.5040 
0.5053 
0.5066 


3.284.^ 
3 245 
31206^^ 


0.3045q7 
0.3082^i 
0.3119^^ 


351 
352 
353 


354 
355 
356 


142.08, Qo 

143.9li^2 
145.75}|4 


325.6 
326.6 

327.7 


1189.9 
1190.2 
1190.5 


864.3 
863.6 
862.8 


781.4 

780.7 
779.8 


82.9 
82.9 
83.0 


0.5078 
0.5091 
0.5104 


3.I680Q 
3.130-^2 
3.092^8 


0.3157oo 
0.3195^° 
0.3234^^ 


354 
355 
356 


357 
358 
359 


147.62. QQ 
149.50!5g 
151.40}^^ 


328.7 
329.7 
330.8 


1190.8 
1191.1 
1191.4 


862.1 
861.4 
860.6 


779.0 

778.3 

777.4 


83.1 
83.1 
83.2 


0.5117 
0.5130 
0.5142 


3.056o« 
3.020'^^ 
2.984| 


0.3272.3Q 

0.331l2n 
O.335I45 


357 
358 
359 


360 


153.33^94 


331.8 


1191.7 


859.9 


776.7 


83.2 


0.5155 


2.94935 


O.339I40 


360 


361 
362 
363 


155.27. Q. 
157.22{^^ 
159.201^8 


332.9 
333.9 
335.0 


1192.0 
1192.4 
1192.7 


859.1 

858.5 
857.7 


775.8 
775.2 
774.3 


83.3 
83.3 

83.4 


0.5168 
0.5181 
0.5193 


2.914o. 
2.880g 
2.846| 


O.343I41 
0.3472*1 

0.3513^2 


361 
362 
363 


364 
365 
366 


161.20^^2 
163.22|^2 


336.0 
337.1 
338.1 


1193.0 
1193.3 
1193.6 


857.0 
856.2 
855.5 


773.5 

772.7 
771.9 


83.5 
83.5 
83.6 


0.5206 
0.5219 
0.5231 


2.813.30 
2.780j^ 
2.748| 


0.3555,0 
O.3597T9 
0.3639^3 


364 
365 
366 


367 
368 
369 


167.3120O 
169.39208 
171.48|^^ 


339.2 
340.2 
341.3 


1193.9 
1194.2 
1194.5 


854.7 
854.0 
853.2 


771.1 
770.4 
769.5 


83.6 
83.6 
83.7 


0.5244 
0.5257 
0.5269 


2.7I601 
2.685^1 
2.654|} 


0.3682,0 
0.3725^^ 
0.37682 


367 
368 
369 


370 


I73.6O214 


342.3 


1194.8 


852.5 


768.7 


83.8 


0.5282 


2.62330 


0.3812^4 


370 


371 
372 
373 


175.742.. 
177.89;!^ 
180.07|lg 


343.3 
344.4 
345.5 


1195.1 
1195.4 
1195.7 


851.8 
851.0 
850.2 


768.0 
767.1 
766.3 


83.8 
83.9 
83.9 


0.5294 
0.5307 
0.5320 


2.534^9 


0.3856,. 
0.3901^^ 
0.3946^^ 


371 
372 
373 


374 
375 
376 


182.27222 
184.49oo7 
186.73|^ 


346.5 
347.5 
348.6 


1196.0 
1196.3 
1196.6 


849.5 

848.8 
848.0 


765.5 
764.8 
763.9 


84.0 
84.0 
84.1 


0.5332 
0.5345 
0.5357 


2.50500 
2.476^o 

2.448| 


0.3992. « 
0.4038;!^ 
0.4084^^ 


374 
375 
376 


377 
378 
379 


188.992^. 
191.27oQ? 
193.58g^ 


349.6 
350.6 
351.7 


1196.9 
1197.2 
1197.5 


847.3 
846.6 
845.8 


763.2 
762.4 
761.6 


84.1 
84.2 
84.2 


0.5370 
0.5382 
0.5395 


2.42O07 

2.393n7 

2.366^^ 


O.413I4. 


377 
378 
379 


380 


195.9I234 


352.8 


1197.8 


845.0 


760.8 


84.2 


0.5407 


2.33825 


0.4276^^ 


380 


381 
382 
383 


198.25^07 
200.62|:g 
203.0lg| 


353.8 
354.9 
355.9 


1198.1 
1198.5 
1198.8 


844.3 
843.6 
842.9 


760.0 
759.3 
758.5 


84.3 

84.3 
84.4 


0.5420 
0.5432 
0.5444 


2.313o« 
2.287^? 
2.262| 


0.4323,0 
0.4372|^ 
0.4421^^ 


381 
382 
383 







SATURATED 


STEAM- 


- Continued. 






ll 

r 

t 


1 

I 1 


If 

O 

1 

9 


S 

o 

A 


1 


1^ 
III 

P 


Jl 

^" o 
Apu 


c ■-> 

fcdt 


o 

S 

s 

I 

1 
c 

5 


Density. 


It 

11 

C X 

E-* 
t 


c c 
7 


384 
385 
386 


205.43-,,. 
210.33^ 


356.9 
358.0 
359.0 


1199.1 
1199.4 
1199.7 


842.2 
&41.4 
840.7 


757.8 
756.9 
756.2 


84.4 
84.5 
84.5 


0..5457 
0.5469 
0.5481 


2.23725 
2.212S- 
2.187- 


0.4470-, 
0.4521^1 
0.4572^1 


384 
385 
386 


387 
388 
389 


215.3l|^^ 


360.1 
361.1 
362.2 


1200.0 
1200.3 
1200.6 


a39.9 
839,2 
838.4 


755.3 
754.6 
758.8 


84.6 
84.6 
84.6 


0.5494 
0.5506 
0.5518 


2.1632, 
2.1395:1 
2.115-^ 


0.4623^2 
0.4675^^ 

0.4728| 


387 
388 
389 


390 


220.3925^ 


363.2 


1200.9 


837.7 


753,0 


84.7 


0.5531 


2.09223 


0.4780-3 


390 


391 
392 
393 


222.96^.^ 
228.19||^ 


364.3 
365.3 
366.4 


1201.2 
1201.5 
1201.8 


836.9 
836.2 
835.4 


752.2 
751.4 
750.6 


84.7 
84.8 
84.8 


0.5543 
0.5555 
0.5568 


2.06923 
2.046^:^ 
2.O24I2 


0.483:3-, 
0.48872J 
0.494r?^ 


391 
392 
393 


394 
395 
396 


230.83„^- 
233.50^^(i 
236.19^2.^ 


367.4 
3G8.4 
369.5 


1202.1 
1202.4 
1202.7 


834.7 
8:34.0 
833.2 


749.9 
749.1 
748.3 


84.8 
84.9 
84.9 


0.5580 
0.5592 
0.5604 


2.00222 

i.98o;; 

1.958^^ 


0.4996-- 
0.5051^^ 
0.5107^3 


394 
395 
396 


397 
398 
399 


238.91274 
241.65|:j^ 


370.5 
371.6 
372.6 


1203.0 
1203.3 
1203.6 


832.5 
831.7 
831,0 


747.6 
746.7 
746.0 


84.9 
85.0 
85.0 


0.5616 
0.5629 
0.5641 


1.937.^, 
1.916;! 
I.8952J 


0.5163.. 
0. 5219^2 
0.5277?^ 


397 
398 
399 


400 


247.21282 


373.7 


1203.9 


830.2 


745.2 


85.0 


0.5653 


1.87420 


0.5336-8 


400 


401 
402 
403 


252.872^:^ 
255.74|^ 


374.7 

375.8 
376.8 


1204.2 
1204.6 
1204.9 


829.5 

828.8 
828.1 


744.5 
743.7 
743.0 


85.0 
85.1 
85.1 


0.5665 
0.5677 
0.5689 


1.8342" 
1.814^^ 


0.5394-Q 

0.5452^g 
0.5112^0 


401 
402 
403 


404 
405 
406 


258.632^2 
264.5029:j 


377.9 
378.9 
380.0 


1205.2 
1205.5 
1205.8 


827.3 
826.6 

825.8 


742.2 
741.4 
740.6 


85.1 

85.2 
85.2 


0.5701 
0.5714 
0.5726 


l-2fl9 
1. no,Q 

1.756}^ 


0.5572^, 
0.5633^^ 
0.5695^1 


404 
405 
406 


407 
408 
409 


267.47ooo 
270.47^'^ 
273.49|gg 


381.0 
382.0 
383.1 


1206.1 
1206.4 
1206.7 


825.1 
824.4 
823.6 


739.9 
739.2 
738.3 


85.2 
85.2 
85.3 


0.5738 
0.5741 
0.5762 


1.737.0 
1.719« 
1.700}^ 


0.5756.2 
0.5818^0 
0.5881^1 


407 
408 
409 


410 


276.543(^8 


384.1 


1207.0 


822.9 


737.6 


85.3 


0.5774 


1.682^8 


0.5945g5 


410 


411 
412 
413 


279.62o.i 
282.73:^1.^ 
285.86^]^ 


385.2 
386.2 
387.3 


1207.3 
1207.6 
1207.9 


822.1 
821.4 
820.6 


736.8 
736.1 
735.3 


85.3 
85.3 
85.3 


0.5786 
0.5798 
0.5810 


1.664.J. 
1.646}^ 
1.629j^ 


0.601. 
0.607? 
0.614^ 


411 

412 
413 


414 
415 
416 


289.02 
292.2l|;^ 

295.42y 


388.3 
389.4 
390.4 


1208.2 

1208.5 
1208.8 


819.9 
819.1 

818.4 


734.5 
733.7 
733.0 


85.4 
85.4 
85.4 


0.5822 
0.5834 
0.5846 


1.612,7 
I.595JI 
1.578}^ 


0.620- 
0.627-1 
0.634,J 


414 
415 
416 


417 
418 
419 


298.67o.,7 
301.94^^^ 
305.24|0 


391.5 
392.5 
393.6 


1209.1 
1209.4 
1209.7 


817.6 
816.9 
816.1 


732.2 
731.5 
730.7 


85.4 
85.4 
85.4 


0.5858 
0.5870 
0.5S81 


1..561i« 
I.545I? 
1.528l^ 


0.641. 
0.647!^ 
0.654J 


417 
418 
419 


420 


308.57333 


394.6 


1210.0 


815.4 


730.0 


85.4 


0.5893 


1.512,3 


O.66I7 


420 


421 
422 
423 


318.73^^^ 


395.6 
390.7 
397.7 


1210,3 
1210.7 
1211.0 


814.7 
814.0 
813.3 


729.3 

728.5 
727.8 


85.4 
85.5 
85.5 


0.5905 
0.5917 
0.5929 


1.496. « 
1.480|^ 
1.465}-, 


0.6680 
0.676? 
0.683| 


421 

422 
423 



10 



SATURATED STEAM — Continued. 






424 
425 
426 

427 
428 






322.1804^ 

325.65^!] 
832. 70o- 



336.26 



356 



5^-l 



39&8 
399.8 
400.9 

401.9 
403.0 



1211.3 
1211.6 
1211.9 

1212.2 
1212.5 



rt> 



812.5 
811.8 
811.0 

810.3 
809.5 



« - - 



727.0 
726.3 
7^5.5 

724.8 
724.0 



Apu 



85.5 
85.5 
85.5 

85.5 
85.5 



J T 



0.5941 
0.5953 
0.5964 

0.5976 
0.5988 



1.449 
1.434 
1.419 

1.404 
1.390 



Density. 



o o s o 



O.69O7 

0.697A 
0.705^ 

0.712^ 
0.719' 






424 
425 
426 

427 
428 



TABLE II. 

SATURATED STEAM. 

ENGLISH TTNITS. 



1 

2 
3 

4 
5 
6 

7 
8 
9 

10 

11 
12 
13 

14 
15 
16 

17 
18 
19 

20 

21 
22 
23 

24 
25 
26 

27 
28 

29 

30 

31 
32 
33 



O C5 



101.99, 
126.27 
141.62 



2428 
1535 
1147 



153.09^25 
162.34'^^^ 
170.14^80 

176.90gQ2 
182.92^^^ 

188.33^^2 



193.25 

197.78 
201.98; 



453 



420 
391 



205.893^3 

209.57om 
213.03^^^ 
216.32^5^^ 

219.44 c^Q 

222.40^2 
225.24^84 

227.95260 

230.55.,5^ 
233.06;^} 
235.472^1 

237.79..-,- 
240.04^:2 



242.21 

244.32, 
246.36 

248.34 

250.27 



217 
211 

204 
198 
193 



188 

252.15.00 
253.9S!^Q 
255.76^^^ 



70.0 

94.4 

109.8 

121.4 
130.7 
138.6 

145.4 
151.5 
156.9 

161.9 

166.5 
170.7 
174.6 

178.3 
181.8 
185.1 

188.3 
191.3 
194.1 

190.9 

199.5 
202.0 
204.5 

206.8 
209.1 
211.2 

213.4 
215.4 
217.4 

219.4 

221.3 
223.1 

224.9 



1113.1 
1120.5 
1125.1 

1128.6 
1131.5 
1133.8 

1135.9 
1137.7 
1139.4 

1140.9 

1142.3 
1143.6 
1144.7 

1145.8 
1146.9 
1147.9 

1148.9 
1149.8 
1150.7 

1151.5 

1152.3 
1153.0 
1153.7 

1154.4 
1155.1 
1155.8 

1156.5 
1157.1 
1157.7 

1158.3 

1158,8 
1159.4 
1159.9 



•^2 



1043.0 
1026.1 
1015.3 

1007.2 

1000.8 

995.2 

990.5 
986. S 
982.5 

979.0 

975.8 
972.9 
970.1 

967.5 
965.1 
962.8 

960.6 
958.5 
956.6 

954.6 

952.8 
951.0 
949.2 

947.6 
946.0 
944.6 

943.1 
941.7 
940.3 

938.9 

937.5 
936.3 
935.0 



981.1 
961.9 
949.5 

940.4 
933.1 
926.7 

921.4 
916.5 
912.4 

908.4 

904.8 
901.5 
898.4 

895.5 
892.6 
890.0 

887.6 

885.3 
883.2 

881.0 

879.0 
877.0 
875.0 

873.2 
871.5 
869.9 

868.2 
866.7 
865.1 

863.6 

862.0 
860.7 
859.2 

12 






Apu 



61.9 
64.2 
65.8 

66.8 
67.7 
68.5 

69.1 
69.7 
70.1 

70.6 

71.0 
71.4 
71.7 

72.0 
72.5 

72.8 

73.0 
73.2 
73.4 



74.0 
74.2 

74.4 
74.5 

74.7 

74.9 
75.0 
75.2 

75.3 

75.5 

75.6 

75.8 



J T 



0.1329 
0.1754 
0.2013 

0.2203 
0.2353 
0.2480 

0.2587 
0.2682 
0.2766 

0.2842 

0.2912 
0.2976 
0.3035 

0.3091 
0.3143 
0.3192 

0.3238 
0.3282 
0.3324 

0.3363 

0.3401 
0.3438 
0.3473 

0.3506 
0.3539 
0.3570 

0.3600 
0.3629 
0.3657 

0.3685 

0.3712 
0.3737 
0.3762 



^^•^'8.30 



53.37 



4o-?o4.94 
'^^•^'^3.97 



38.I6328 

o4.88q y^A 

29.82£2^ 

26.10, .,, 
24.59}j^ 



23.22 

22.00 
20.90, 

19.91 

19.01 

IS. 20; 

17.45* 

16.76. 
16.13, 
15.55t 



1.22 
1.10 
0.99 



90 



81 



15.00.^ 
14.49^J 
i4.03|^ 



13.59 

13.18 
12.78 
12.41 



Density. 



•Sf = o o 

« O s o 



0.0029927- 
0.00576y'^ 
0.00&44^| 

0.01107.,5C) 
0.01366-?p 
0.016225^ 

0.01874.^. 

0.02125^5o 
0.02374|^^ 

O.O262I245 

0.02866.,,^ 
0.03111^2 
0.03355-45 

0.03600o.-.p 

0.03826^^V 
0.0406724Q 

0.0430724O 
0.04547;^[^ 
0.047S6g;^ 

0.05023or,/. 

0.05259.^or 
0.05495-:^P 
0.0573l|g 

0.05966.^00 
0.06199^0 
0.06432-g4 

O.O6666..0Q 
0.06899^0, 
0.07130|J 

0.0736023Q 

0.07590ooi 
0.07821;:^;, 
0.08051-'^^ 



SATURATED STB AM— Continued, 



34 
35 
36 

37 
38 
39 

40 

41 
42 
43 

44 
45 
46 

47 
48 
49 

50 

51 
52 
53 



55 
56 

57 



60 

61 
62 
63 

64 
65 
66 

67 
68 
69 

70 

71 
72 
73 






1^ 
Eh 

t 



257.50 
259.19 
260.8e 



169 
166 
162 



262.47^59 
264.06!^r 
265.61}'^^ 

267.13^49 

26^.62j^g 

271.5l||^ 

272.91. oo 
274.29^g 
275.65||^ 

276.99. qi 
278.30^^0 
279.58i|« 

280.85^25 

282.10. ..o 
283.32|^f 
284.53|^1 



54 I 285.72 



286.^ 
288.05 

289.19 

58 290.31 

59 291.42 



292.51 



117 
116 
114 

112 
111 
109 

108 



295.70}^^ 

296.74,.o 
297.77^^^ 



298.78, 

299.77, 
300.76; 
301.74; 



101 
99 



302.71^5 

303.66q. 
304.61qo 
305.54^^ 



226.7 
228.4 
230.0 

231.7 
233.3 
234.8 

236.4 

237.9 
239.3 
240.8 

242.2 
243.6 
245.0 

246.3 
247.6 

248.9 

250.2 

251.5 
2.52.7 
253.9 

2.55.1 
256.3 
257.5 

258.6 
259.7 
260.8 

261.9 

263.0 
264.1 

265.2 

266.2 
267.2 
268.3 

269.3 
270.3 
271.2 

272.2 

273.2 
274.1 
275.1 



1160.4 
1161.0 
1161.5 

1162.0 
1162.5 
1163.0 

1163.4 

1163.9 
1164.3 
1164.8 

116.5.2 
1165.6 
1166.0 

1166.4 
1166.8 
1167.2 

1167.6 

1168.0 
1168.4 
1168.7 

1169.1 
1169.4 
1169.8 

1170.1 
1170.5 
1170.8 

1171.2 

1171.5 
1171.8 
1172.1 

1172.4 
1172.7 
1173.0 

1173.3 
1173.6 
1173.9 

1174.3 

1174.6 
1174.9 
1175.2 



o o. 



933.7 
932.6 
931.5 

9.30.3 
929.2 
928.2 

927.0 

926.0 
925.0 
924.0 

92.3.0 
922.0 
921.0 

920.1 
919.2 
918.3 

917.4 

916.5 
915.7 
914.8 

914.0 
913.1 
912.3 

911.5 

910.8 
910.0 

909.3 

908.5 
907.7 
906.9 

906.2 
905.5 
904.7 

904.0 
903.3 
902.7 

902.1 

901.4 

900.8 
900.1 



O - i. 

P 



857.8 
856.6 
855.3 

854.0 
852.8 
851.7 

850.3 

849.2 
848.1 
847.0 

845.9 
844.8 
843.7 

842.7 
841.7 
840.7 



838.7 
837.8 
836.8 

835.9 
834.9 
834.0 

833.1 
832.4 
831.5 

830.7 

829.8 
828.9 
828.0 

827.3 
826.5 
825.6 

824.8 
824.1 
823.4 

82^7 

821.9 

821.3 
820.5 









75.9 
76.0 
76.2 

76.3 
76.4 
76.5 

76.7 

76.8 
76.9 
77.0 

77.1 

77.2 
77.3 

77.4 
77.5 
77.6 

77.7 

77.8 
77.9 
78.0 

78.1 
78.2 
78.3 

78.4 

78.4 
78.5 

78.6 

78.7 
78.8 
78.9 



79.0 
79.1 

79.2 
79.2 
79.3 

79.4 

79.5 
79.5 



rcdt 



0..3787 
0.3811 
0.3834 

0..3856 
0.3878 
0.3900 

0.3921 

0.3942 
0.3962 
0.3982 

0.4001 
0.4020 
0.4038 

0.4056 
0.4074 
0.4092 

0.4109 

0.4126 
0.4143 
0.4160 

0.4175 
0.4191 
0.4207 

0.4222 
0.4237 
0.4252 

0.4267 

0.4281 
0.4295 
0.4309 

0.4323 
0.4337 
0.4350 

0.4363 
0.4376 
0.4389 

0.4402 

0.4415 
0.4428 
0.4440 



12.07, 
11.75! 
11.45! 



II.I60Q 

10.88^^ 
10.622- 



10.37 

10.13. 

9.906; 
9, 

9.484 
9.287 
9.097 



24 

22 
216 

206 

197 
190 
183 



8.914^^ 
8.740|^^ 
8.573^J 



8.414 

8.2.59 
8.110 
7.968 

7.829. 00 
7. 696^^5 

7.568ji 



155 

149 
142 
138 



7.443 
7.323 



7.( 



120 
115 
'112 

'109 



6.987io3 
6.882j^^ 
6.779^^3 



6.680. 
6.583 
6.490; 

6.401 
6.314 
6.228! 



6.144si 

6.063-Q 

5.984{^ 
5.908i^ 



Density, 



^P -P 



0.08280^^0 
0.08508^^^ 
0.08736223 

0.08964...^^ 
0.091913^' 
0.09417|^ 

0.09644.,... 
22o 

0.09869.,.,-, 

0.1009.,o 

0.103222 

0.1054.,., 
0.10775^ 
0.10992 J 

0.1122.,^ 
0.1144;r> 
O.II6625 



0.1188, 

0.1211 
0.1233 
0.1255 

0.1277. 
0.1299' 



0.1321 



23 



0.1344.,^ 
0.1366;^ 
0.1387-5^ 

0.140922 

0.1431.-,=, 
0.14.535^ 
O.I4752I 

0.1497.,., 
0.1519^; 
0.154l2f 

0.156222 



0.1584; 



0.1606: 



22 



22 



O.I62821 

0.1649.-,o 
0.1671|:^ 
0.16932]^ 



34 
35 
36 

37 
38 
39 

40 

41 
42 
43 

44 
45 
46 

47 
48 
49 

50 

51 
52 
53 

54 
55 
56 

57 
58 
59 

60 

61 
62 
63 

64 
65 
66 

67 
68 
69 

70 

71 
72 
73 



13 



SATURATED STEAM- 



Continued. 



74 
75 
76 

77 
78 
79 

80 

81 
82 
83 

84 
85 
86 

87 
88 
89 

90 

91 
92 
93 

94 
95 
96 

97 
98 

99 

100 

101 
102 
103 

104 
105 
106 

107 
108 
109 

110 

111 
112 
113 



28 



306.46, 
307.38, 
308.28; 



309.18, 
310.06 
310.94 



88 



311.80gg 

31 2. 66q> 
313.5l5'? 
314.36oo 



315.19qo 

316.02^^ 
316.84^2 

317. 



;80 



79 



318.45; 
319.25; 

320.04^^ 

320.83-^ 
321.00i.i 
3->2 37'' 

323. 14- 

323.89i9 

324.64^^ 

325.38^. 
326.121; 
326.86^1 

327.58-2 



328.30-. 
329.02if 
329.73^1 



330.43-. 
331.13'^ 
331.83^^0 

332.52 

333.20^^ 

333.88^8 



3:34.56, 



67 



335.23, 
335. 89| 
336.55, 



276.0 
276.9 
277.8 

278.7 
279.6 
280.5 

281.4 

282.3 
283.2 
284.1 

285.0 

285.8 
286.7 

287.5 
288.4 
289.2 

290.0 

290.8 
291.6 
292.4 

293.2 
294.0 
294.8 

295.6 
296.4 
297.1 

297.9 

298.6 
299.4 
300.1 



1175.4 
1175.7 
1176.0 

1176.2 
1176.5 
1176.8 

1177.0 

1177.3 
1177.6 
1177.8 

1178.1 
1178.3 
1178.6 

1178.8 
1179.1 
1179.3 

1179.6 

1179.8 
1180.0 
1180.3 

1180.5 
1180.7 
1181.0 

1181.2 
1181.4 
1181.6 

1181.9 

1182.1 
1182.3 
1182.5 



300.9 1182.7 
301.6 1182.! 
302.3 1183.1 



302.0 
303.8 
304.5 

305.2 

305.9 
306.6 
307.3 



1183.4 
1183.6 
1183.8 

1184.0 

1184.2 
1184.4 
1184.6 



899.4 819.7 
898.8 819.1 
898.2 818.4 



897.5 
896.9 
896.3 

895.6 

895.0 
81)4.4 
893.7 



893.1 812.8 
892.5 812.1 
L.9 811.5 



817.6 
817.0 
816.3 

815.5 

814.0 
814.2 
813.4 






Apu 



(cdt 
J T 



891.3 
890.7 
890.1 

889.6 

889.0 

888.4 
887.9 

887.3 
886.7 
886.2 

885.6 
885.0 
884.5 

884.0 

883.5 
882.9 
882.4 

881.8 
881.3 
880.8 

880.4 
879.8 
879.3 

878.8 

878.3 
877.8 
877.3 



810.8 
810.2 
809.5 

808.9 

808.3 
807.6 
807.1 

806.4 

805.8 
805.2 

804.6 
803.9 
803.4 

802.8 

802.3 
801.6 
801.1 

800.4 
799.9 
799.3 

798.9 
798.2 
797.7 

797.1 

796.6 
796.1 
795.5 



79.7 
79.7 
79.8 

79.9 
79.9 
80.0 

80.1 

80.1 
80.2 
80.3 

80.3 
80.4 
80.4 

80.5 
80.5 
80.6 

80.7 

80.7 
80.8 
80.8 



0.4452 
0.4464 
0.4476 

4487 
0.4499 
0.4511 

0.4522 

0.4.534 
0.4.545 
0.4557 

0.4.568 
0.4.579 
0.4590 

0.4601 
0.4612 
0.4622 

0.4633 

0.4643 
0.4653 
0.4663 



80 9 0.4673 
80.9 0.4083 
81.0 0.4693 



81.0 
81.1 
81.1 

81.2 

81.2 
81.3 
81.3 

81.4 
81.4 
81.5 

81.5 
81.6 
81.6 

81.7 

81.7 
81.7 
81.8 



0.4703 
0.4713 
0.4723 

0.4733 

0.4743 
0.4753 
0.4762 

0.4771 
0.4780 
0.4790 

0.4799 
0.4808 
0.4817 

0.4826 

0.4835 
0.4843 
0.4852 



5.834-2 
5.762if 
5.691^1 



5.621 
5.554 

5.488| 

5.425, 
5..362 



67 



63 



5.301 
5.240 



5.182-- 

5.125'?^ 
5.009^^6 

5.014 

4.96lg 

4.909^^ 

4.858,() 

4.808, Q 

4.76CJ5 
4.712^^ 



4.665 
4.619' 
4.574 



4.530 

4.486' 
4.444' 



4.403^1 

4.362,^ 
4.322^^ 

4.282^0 

4.244oo 
4.206:^2 
4.169|^ 

4.132..^ 



4.096; 
4.061; 



4.02634 

3.992.5.3 

3.959:J^ 
3.926!^^ 



Density. 



.r - a, o 
G c g o 



0.1714 



70^22 



0.1 
0.1757 



22 

0.17792P 
O.lSOl^f 
0.1822^ J 



0.1843 



22 



0.1865 



0.1886; 
0.1908; 

0.1930. 
0.1951 
0.1973; 



0.1994^2 
0.2016^7 
0.2037^1 

0.205822 

0.2080„. 
0.2101^1 
0.212221 



0.2144 



0.2165- 



21 



0.2186; 

2208 
0.2229^ 



21 



0.2250; 



rX21 



21 



0.2271 



22 



0.2293 



0.2314, 



21 



0.233 



41 



0.2356 
0.2378: 
0.2399; 



0.2420, 
0.2441; 
0.2462; 



0.24842^ 

0.2505^1 
0.2526^1 
0.254725 



74 
75 
76 

77 
78 
79 

80 

81 
82 
83 

84 
85 
86 

87 
88 
89 

90 

91 
92 
93 

94 
95 
96 

97 
98 
99 

100 

101 
102 
103 

104 
105 
106 

107 
108 
109 

110 

111 
112 
113 



li 



SATURATED STB AM — Continued. 



ft 

5 ^ 


i 



1 


1 

2 

Eh 


.1 

1 

^ a 
H 


Heat equivalent 
of Internal 
Work. 


1^ 


2 

=1 

r 


a 

3 

> 

1 


Density. 


1 

-= - 

= ;£ 2. 
1 1 




/ 


/ 


? 


\ 


r 


P 


Apu 


(cdt 
J"7^ 


J 


V 


P 


114 
115 
116 


337.80^7 
338.50^J 


308.0 
308.7 
309.4 


1184.8 
1185.0 
1185.2 


876.8 
876.3 
875.8 


795.0 
794.4 
793.9 


81.8 
81.9 
81.9 


0.4860 
0.4869 
0.4877 


3.894.30 
3.862:^f 
3.83r|J 


0.2568.,-, 
0.2589^1 
O.26IO2J 


114 
115 
116 


117 
118 
119 


339.14.. 
339.78^^ 
340.42^1 


310.0 
310.7 
311.4 


1185.4 
1185.6 
1185.8 


875.4 
874.9 
874.4 


793.5 
792.9 
792.4 


81.9 
82.0 
82.0 


0.4886 
0.4894 
0.4903 


3.801qi 

3.770^J 
3.740^^ 


0.2631^^ 
0.2653^f 
0.2674|j 


117 
118 
119 


120 


341.05^2 


312.0 


1186.0 


874.0 


791.9 


82.1 


0.4911 


3.71I28 


0.26952Q 


120 


121 
122 
123 


341.67..^ 
342.29^2 

342.91^- 


312.7 
313.3 
314.0 


1186.2 
1186.3 
1186.5 


873.5 
873.0 
872.5 


791.4 
790.8 
790.3 


82.1 

82.2 
82.2 


0.4919 
0.4927 
0.4935 


3.683.,. 

3-6pi 
3.62*28 


0.271521 
0.2736^1 
0.2757g 


121 
122 
123 


124 
125 
126 


343.52.. 
o44.,og(j 


314.6 
315.2 
315.9 


1186.7 
1186.9 
1187.1 


872.1 
871.7 
871.2 


789.9 
789.4 
788.9 


82.2 
82.3 
82.3 


0.4943 
0.4951 
0.4959 


3.599.,^ 
3.572^^ 
3.546^ 


0.27793. 
0.2800; A 
0.2820|^ 


124 
125 
126 


127 
128 
129 


345.33.^ 

345.93^;0 

346.53^^^ 


316.5 
317.1 

318.7 


1187.3 
1187.4 
1187.6 


870.8 
870.3 
869.9 


788.4 
787.9 

787.5 


82.4 
82.4 
82.4 


0.4967 
0.4974 
0.4982 


3.520.-,« 
3.494g 
3.469| 


0.2841^, 
0.2862;| 
0.2883|| 


127 
128 
129 


130 


347.12.^ 


318.4 


1187.8 


869.4 


786.9 


82.5 


0.4990 


3.444^5 


0.290421 


130 


131 
132 
133 


347.7U. 
348.292^ 
348.87g 


319.0 
319.6 
320.2 


1188.0 

1188.2 
1188.4 


869.0 

868.6 
868.2 


786.5 
786.1 
785.6 


82.5 
82.5 
82.6 


0.4997 
0.5005 
0.5012 


3.419 , 
3.395;^ 
3.371|| 


0.2925.,, 
0.2946;{ 
0.29672J 


131 
132 
133 


134 
135 
136 


349.45>Q 
350.03'?2 
350.60g| 


320.8 
321.4 
322.0 


1188.5 
1188.7 
1188.9 


867.7 
867.3 
866.9 


785.1 

784.7 
784.2 


82.6 
82 6 

82.7 


0.5020 
0.5027 
0.5035 


3.347.,, 
3.323-| 
3.300^3 


0.298821 
0. 3009^1 
0.3030|j 


134 
135 
136 


137 
138 
139 


351.17^. 
351.73?^ 
352.29^?^ 


322.6 
323.2 
323.8 


1189.0 
1189.2 
1189.4 


866.4 
866.0 
865.6 


783.7 
783.3 

782.8 


82.7 
82.7 
82.8 


0.5042 
0.5049 
0.5056 


3.27722 
3.255^f 
3.234|^ 


0.305U. 
0.3072;i. 
0.3092^^ 


137 
138 
139 


140 


352.85^, 


324.4 


1189.5 


865.1 


782.3 


82.8 


0.5064 


3.2122^ 


0.311321 


140 


141 
142 
143 


353.40.^ 
353.95?'? 
354.50- 


325.0 
325.6 
326.1 


1189.7 
1189.9 
1190.1 


864.7 
864.3 
864.0 


781.9 
781.4 
781.1 


82.8 
82.9 
82.9 


0.5071 
0.5078 
0.5085 


3.191^. 
3.170^1 
3.149|} 


0.3134^-, 
0.3155;j 
0.317621 


141 
142 
143 


144 
145 
146 


355.05- t 
355.59'?t 
356.13^^ 


326.7 
327.2 
327.8 


1190.2 
1190.4 
1190.6 


863.5 
863.2 
862.8 


780.6 
780.2 
779.8 


82.9 
83.0 
83.0 


0.5092 
0.5099 
0.5106 


3.1282. 
3.107|J 
3.087g 


0.3197^-, 
0.3218;i 
0.3239|J 


144 
145 
146 


147 
148 
149 


356.67.0 
357.20'^:^ 
357.73- 


328.3 
328.9 
329.4 


1190.7 
1190.9 
1191.0 


862.4 
862.0 
861.6 


779.4 

778.9 

778.5 


83.0 
83.1 
83.1 


0.5113 
0.5119 
0.5126 


3.068.O 
3.049|^ 
3.030J^ 


0.3259.,-, 
0.3280;/. 
0.3300|j 


147 
148 
149 


150 


358.2652 


330.0 


1191.2 


861.2 


778.1 


83.1 


0.5133 


3.011^9 


O.332I21 


150 


151 
152 
153 


358.78.., 
359.30'?; 
359.82- 


330.5 
331.1 
331.6 


1191.4 
1191.5 
1191.7 


860.9 
860.4 
860.1 


777.7 
777.2 
776.9 


83.2 
83.2 
83.2 


0.5140 
0.5146 
0.5153 


2.992.q 
2.973{^ 
2.955JI 


0.334221 
0.3363;| 
0.3384|} 


151 
152 
153 



15 



SATURATED STB A.M—ContimieJ. 



l 

m 


,-5 


o 

1 


1 

A 


I 

1 

r 

r 


L 


1- 


11 

[cdt 


Si 

S 

I 

1 


Density. 




11 
p 


11 
Apu 


i 

V 


154 
155 
156 


360.862f 
361.37^1 


332.2 
332.7 
333.3 


1191.8 
1192.0 
1192.2 


859.6 
859.3 
858.9 


776.3 
776.0 
775.6 


83.3 
83.3 
83.3 


0.5160 
0.5166 
0.5173 


2.937.g 
2.919{J 
2.90lj!^ 


0.3405^. 
0.:3426^} 
0.3447^J 


154 
155 
156 


157 
158 
159 


3G1.88.. 
362.39'?} 
362.90^1 


333.8 
334.3 
334.9 


1192.3 

1192.5 
1192.7 


858.5 
858.2 
857.8 


775.2 

774.8 
774.4 


83.3 
83.4 
83.4 


0.5179 
0.5186 
0.5192 


2.884. 
2.867i4 
2.850|| 


0..3467^. 
O.34882I 
0.3509^ J 


157 
158 
159 


160 


363.40^^^ 


335.4 


1192.8 


857.4 


774.0 


83.4 


0.5198 


2.833,^ 


O.353O21 


160 


161 
162 
163 


303.90 

364.40'^X 
364.90^^ 


335.9 
336.4 
337.0 


1193.0 
1193.1 
1193.3 


857.1 
856.7 
856.3 


773.7 
772.2 

7T2.S 


83.4 
83.5 
83.5 


0.5205 
0.5211 
0.5217 


2.816 . 
2.799}; 
2.783}« 


0.3551^. 
0.:3572|| 
0.3593|} 


161 
162 
163 


164 
165 
166 


3G5.39^^ 
365.88^^, 
366.37^^ 


337.5 

338.0 
338.5 


1193.4 
1103.6 
1193.7 


855.9 
855.6 
855.2 


772.4 
772.0 
771.6 


83.5 
83.6 
83.6 


0.5224 
0.52:30 
0.5236 


2.767.. 
2.75l{^^ 
2.736}^ 


0.3614 . 
0.3635f,/. 
0.:3655f^ 


164 
165 
166 


167 
168 
169 


366.85. Q 
367.33;i| 
367.81^^ 


339.0 
339.5 
340.0 


1193.9 
1194.0 
1194.2 


854.9 
854.5 
854.2 


771.3 

770.9 
770.5 


83.6 
83.6 
83.7 


0.5242 

0.5248 
0.5254 


2.721 

2.706}'^ 

2.69l}^ 


0.3675^^ 
0.3695^Y 
O.37I62J 


167 
168 
169 


170 


368.29^g 


340.5 


1194.3 


853.8 


770.1 


83.7 


0.5260 


2.676^, 


0.3-3721 


170 


171 
172 
173 


868.77,^ 
369.2474 
369.71^^ 


341.0 
341.5 
342.0 


1194.4 
1194.6 
1194.7 


853.4 
853.1 
852.7 


769.7 
769.4 
768.9 


8:^.7 
83.7 
83.8 


0.5266 
0.5272 
0.5278 


2.661 , 
2.647}^ 
2.632J2 


0..j< (b.-), 
0.3799|J 


171 
172 
173 


174 
175 
176 


370.18,^ 
370.05^4 
371. 12^ j 


342.5 
343.0 
343.5 


1194.8 
1195.0 
1195.1 


852.3 
852.0 
851.6 


768.5 

768.2 
767.8 


83.8 
83.8 
8:3.8 


0.5284 
0.5290 
0.5296 


2.618,- 
2.603i7 
2.589l| 


0.3820^. 
0.;3841^J 
0.3862^ J 


174 
175 
176 


177 
178 
179 


371.59,. 
372.05^^ 
372.51^^ 


344.0 
344.4 
344.9 


1195.3 
1195.4 
1195.6 


851.3 
851.0 
850.7 


767.5 
767.1 
766.8 


83.8 
8:3.9 
83.9 


0.5302 
0.5:308 
0.5313 


2.575., 
2.56l|^ 
2.548j^ 


0.3883.,, 
0.3004^1 
0.3925^^ 


177 
178 
179 


180 


372.97,3 


345.4 


1195.7 


850.3 


766.4 


83.9 


0.5319 


2.535^3 


0.39452, 


180 


181 
182 
183 


373.43,. 
373.887^ 
374.33|9 


345.9 
346.4 
346.8 


1195.9 
1196.0 
1196.1 


850.0 
849.6 
849.3 


766.1 
765.6 
765.3 


83.9 
84.0 
84.0 


0.5325 
0.5:331 
0.5336 


2.522, 
2.508j^ 
2.495^1 


0.3966., 

0.:3987^t 
0.4008^, 


181 
182 
183 


184 
185 
186 


374.78,- 
375.231? 
375.68^ 


347.3 

347.8 
348.2 


1196.2 
1196.4 
1196.5 


848.9 
848.6 
848.3 


7&4.9 
764.6 
764.3 


84.0 
84.0 
84.0 


0.5342 
0.5:347 
0.5353 


2.482 

2.470}^ 

2.457II 


0.4029^. 
0.4049.f/ 
0.4070^i 


184 
185 
186 


187 
188 
189 


376.12^ 
376.56T7 
377.00JJ 


348.7 
349.2 
349.6 


1196.6 
1196.8 
1196.9 


847.9 
847.6 
847.3 


763.8 
763.5 
763.2 


84.1 
84.1 
84.1 


0.5359 
0.5364 
0.5370 


2.445^o 
2.4:32{| 
2.420^1 


0.4090.^, 
0.4111;! 
0.4132|J 


187 
188 
189 


190 


377.44,, 


350.1 


1197.1 


847.0 


762.9 


84.1 


0.5375 


2.408,2 


0.41532, 


190 


191 
192 

193 


377.88^ 
378.321^ 
378.75JJ 


350.5 
351.0 
351.4 


1197.2 
1197.3 
1197.4 


846.7 
846.3 
846.0 


762.5 
762 1 
761.8 


84.2 
84.2 
84.2 


0.5381 
0..5;386 
0.5:391 


2.396,, 
2.:385J^ 

^•"'"12 


0.41742Q 
0.4194;V 
0.42152, 


191 
192 
193 



16 



SATURATED STB AM— Continued. 



i 
.11 

Pi 

V P 


i 

i 


."2 

1 


1 

A 


□ 
.2 


P 


III 

Apu 


M 

25 

a 

[cdt 
J T 




a 

s 

I 



•1 


Density. 


3^ 

Pi 

I I- 


.2f5 1, 

S s 

V 


194 
195 
196 


379. 18. o 
379.6IT0 
380.04J^ 


351.9 
352.4 
352.8 


1197.6 
1197.7 
1197.8 


845.7 
845.3 
845.0 


761.5 
761.1 
760.8 


84.2 
84.2 
84.2 


0.5397 
0.5402 
0.5408 


2.361. „ 
2.349j^ 
2.337i| 


0.4236.,, 
0.42571^ 
0.4278^J 


194 
195 
196 


197 
198 
199 


380.897^ 
381.31^ 


353.3 
353.7 
354.1 


1198.0 
1198.1 
1198.2 


844.7 
844.4 
844.1 


760.4 
760.1 
759.8 


84.3 
84.3 
84.3 


0.5413 
0.5418 
0.5423 


2.325 

2.314{1 

2.304IO 


0.4298..^ 
0.4318;^ 
0.4338|^ 


197 
198 
199 


200 


381.73^2 


354.6 


1198.4 


843.8 


759.5 


84.3 


0.5429 


2.294^, 


0.43592Q 


200 


201 
202 
203 


382.15, 

382.57^1 

382.992 


355.0 
355.4 
355.9 


1198.5 
1198.6 
1198.8 


843.5 
843.2 
842.9 


759.1 

758.8 
758.5 


84.4 
84.4 
84.4 


0.5434 
0.5439 
0.5444 


2.284 

2.274^,^ 

2.263jj 


0.4379^0 
0.4399SV 
0.4420|^ 


201 
202 
203 


204 
205 
206 


383.41,; 
383.827; 
384.23|J 


356.3 
356.8 
357.2 


1198.9 
1199.0 
1199.1 


842.6 

842.2 
841.9 


758.2 
757.8 
757.4 


84.4 
84.4 
84.5 


0.5449 
0.5454 
0.5459 


2.252 

2.241II 

2.231JO 


0.4441,^^ 
0.4461^0 
0.4482-} 


204 
205 
206 


207 
208 
209 


384.64,. 
380.057! 
385.46|J 


357.6 
358.0 
358.5 


1199.3 
1199.4 
1199.5 


841.7 
841.4 
841.0 


757.2 
756.9 
756.5 


84.5 
84.5 

84.5 


0.5465 
0.5470 
0.5475 


2.221 

2.21liY 

2.200JI 


0.4503^, 
0.4524;1 
0.4544^5 


207 
208 
209 


210 


385.87^^ 


358.9 


1199.6 


840.7 


756.2 


84.5 


0.5480 


2.190,, 


0.45652, 


210 


211 
212 
213 


386.28,^ 
386.687X 
387.08|^ 


359.3 
359.7 
360.1 


1199.8 
1199.9 
1200.0 


840.5 
840.2 
839.9 


756.0 
755.6 
755.3 


84.5 
84.6 
84.6 


0.5485 
0.5489 
0.5494 


2.I8O0 
2.171^ 
2.162^, 


0.4586^. 
0.4607^^ 
0.4627^0 


211 
212 
213 


214 
215 
216 


387.48,. 
387.887X 
388.28^^ 


360.6 
361.0 
361.4 


1200.1 
1200.2 
1200.4 


839.5 

839.2 
839.0 


754.9 
754.6 
754.4 


84.6 
84.6 
84.6 


0.5499 
0.5504 
0.5509 


2.152 

2.142|^ 

2.132^^ 


0.4648 , 
0.4669^1 
0.4690^} 


214 
215 
216 


217 
218 
219 


388.67oQ 
389.06:^^ 
389.45^ 


361.8 
362.2 
362.6 


1200.5 
1200.6 
1200.7 


838.7 
838.4 
838.1 


754.1 

753.8 
753.4 


84.6 
84.6 

84.7 


0.5514 
0.5519 
0.5524 


2.123 

2.114^ 

2.105^ 


0.4711 

0.4731^^ 

0.4751^0 


217 
218 
219 


220 


389.843^ 


363.0 


1200.8 


837.8 


753.1 


84.7 


0.5529 


2.096g 


0.47722, 


220 


221 
222 
223 


390.23.30 
390.62!^^ 
391.0l| 


363.5 
363.9 
364.3 


1201.0 
1201.1 
1201.2 


837.5 
837.2 
836.9 


752.8 
752.5 

752.2 


84.7 
84.7 
84.7 


0.5533 
0.5538 
0.5543 


2.087 

2.078;^ 

2.069^ 


0.4792 . 
0.4813|j 
0.4834|J 


221 
222 
223 


224 
225 
226 


391.40.30 
391.79!^^ 
392.17| 


364.7 
365.1 
365.5 


1201.3 
1201.4 
1201.6 


836.6 
836.3 
836.1 


751.9 

751.6 
751.3 


84.7 

84.7 
84.8 


0.5548 
0.5553 
0.5557 


2.O6O0 
2.051^ 
2.042^ 


0.4855 

0.4876^i 

0.4896^} 


224 
225 
226 


227 
228 
229 


392.55qQ 
392.93:5^ 
393.3l| 


365.9 
366,3 
366.7 


1201.7 
1201.8 
1201.9 


835.8 
835.5 
835.2 


751.0 

750.7 
750.4 


84.8 
84.8 
84.8 


0.5562 
0.5567 
0.5571 


2.034q 
2.026^ 
2.017^ 


0.4917.0 
0.4939^X 
0.4959-, 


227 
228 
229 


230 


393.6933 


367.1 


1202.0 


834.9 


750.1 


84.8 


0.5576 


2.009g 


9.49792, 


230 


231 
232 
233 


394.07.3Q 
394.45:'5 

394.82:^^ 


367.5 
367.9 
368.3 


1202.1 
1202.2 
1202.4 


834.6 
834.3 
834.1 


749.8 
749.5 

749.2 


84 8 
84.8 
84.9 


0.5581 
0.5585 
0.5590 


2.001 

1.992^ 

1.984g 


0.5000^. 
0.5021;;. 
O.504I2, 


231 
232 
233 



17 







SATURATED 


STEAM- 


- Continued, 






1 

■i-s 

1 i 


d 
II 


3 

3 
1 


1 
1 


a 
"3 

1^ 




11 

is . 

1°^ 


'6 


6 

I 

s 

1 


Density. 


1 

.11 

n 




p 


t 


7 


A. 


r 


p 


A/u 


fcdt 
J T 


J 


y 


P 


234 
235 
236 


395.19.3^ 
395.56:^4 
395.93^1 


368.6 
369.0 
369.4 


1202.5 
1202.6 
1202.7 


833.9 
833.6 
833.3 


749.0 

748.7 
748.4 


84.9 
84.9 
84.9 


0.5594 
0.5599 
0.5603 


1.976g 


0.506220 
0.5082^V 
0.510321 


234 
235 
236 


237 
238 
239 


396.30.3- 
396.6To4 
397.04^1 


369.8 
370.2 
370.6 


1202.8 
1202.9 
1203.0 


833.0 
832.7 
832.4 


748.1 
747.8 
747.5 


84.9 
84.9 
84.9 


0.5608 
0.5612 
0.5617 


1.952q 
1.944^ 
1.936g 


0.5123.^. 
0.5144^J 
0.5165^J 


237 
238 
239 


240 


397.4l3g 


371.0 


1203.2 


832.2 


747.3 


84.9 


0.5621 


1.928^ 


O.5I862Q 


240 


241 
242 
243 


39T.77o« 
398.13:;^^ 
398.49^^ 


371.3 
371.7 
372.1 


1203.3 
1203.4 
1203.5 


832.0 
831.7 
831.4 


747.0 
746.7 
746.4 


85.0 
85.0 
85.0 


0.5626 
0.5630 
0.5635 


1.921ft 
1.913? 
1.906^ 


0.5206..^ 
0.5226;y 
0.5247^j 


241 
242 
243 


244 
245 
246 


398.85.3« 
399.2i:^^ 
399.57^^ 


372.5 
372.8 
373.2 


1203.6 
1203.7 
1203.8 


831.1 
830.9 
830.6 


746.1 
745.9 
745.6 


85.0 
85.0 
85.0 


0.5639 
0.5643 
0.5648 


1.898- 
1.891^ 
1.883^ 


0.5268^. 
0.5289^i 
0.5311^^ 


244 
245 
246 


247 
248 
249 


399.93op 
400.29:^!? 
400.64g 


373.6 
374.0 
374.3 


1203.9 
1204.0 
1204.1 


830.3 
830.0 
829.8 


745.3 
745.0 
744.8 


85.0 
85.0 
85.0 


0.5652 
0.5650 
0.5661 


1.875„ 
1.868;^ 
1.861J 


0.5332..1 
0.5353SA 
0.5373-^ 


247 
248 
249 


250 


400.9935 


374.7 


1204.2 


829.5 


744.5 


85.0 


0.5665 


1.854^ 


0.53932Q 


250 


251 
252 
253 


401.34.3- 
4U1.69f? 
402.04^^ 


375.1 
375.4 

375.8 


1204.4 
1204.5 
1204.6 


829.3 
829.1 
828.8 


744.2 
744.0 
743.7 


85.1 
85.1 
85.1 


0.5669 
0.5673 
0.5678 


1.847- 
1.8404 
1.833| 


0.5413;,^ 
0.5433;Y 
0.5454|{ 


251 
252 
253 


254 
255 
256 


402.39.3- 
402. 74f? 
403.09g 


376.2 
376.5 
376.9 


3204.7 
1204.8 
1204.9 


828.5 
828.3 
828.0 


743.4 
743.2 
742.9 


85.1 
85.1 
85.1 


0.5682 
0.5686 
0.5690 


1.826- 
1.819i 
1.812| 


0.547521 
0.5496^} 
0.55172} 


254 
255 
256 


257 
258 
259 


403.44.,- 
403.79:^^ 
404.13^^ 


377.3 
377.6 
378.0 


1205.0 
1205.1 
1205.2 


827.7 
827.5 
827.2 


742.6 
742.4 
742.1 


85.1 
85.1 
85.1 


0.5695 
0.5699 
0.5703 


1.805- 
1.798' 
1.792^ 


0.5538^. 
0.5559;} 
0.5580^J 


257 
258 
259 


260 


404.473^ 


378.4 


1205.3 


826.9 


741.7 


85.2 


0.5707 


1.785g 


0.560120 


260 


261 
262 
263 


404.8I0, 
405.49^^ 


378.7 
879.1 
379.4 


1205.4 
1205.5 
1205.6 


826.7 
826.4 
826.2 


741.5 
741.2 
741.0 


85.2 
85.2 
85.2 


0.5711 
0.5715 
0.5719 


1.779. 
1.773? 

1.766J 


0.5621^. 
0.5642^1 
0.5663|} 


261 
262 
263 


264 
265 
266 


405.83.3. 
406.17:3: 
406.5lg 


379.8 
3S0.2 
380.5 


1205.7 
1205.8 
1205.9 


825.9 
825.6 
825.4 


740.7 
740.4 
740.2 


85.2 
85.2 
85.2 


0.5724 
0.5728 
0.5732 


1.759p^ 
1.753? 
1.746^ 


0.5684o-, 
0.5705t| 
0.5726^J 


264 
265 
266 


267 
268 
269 


406.84.3_, 
407.180: 
407.52^^ 


380.8 
381.2 
381.5 


1206.0 
1206.1 
1206.2 


825.2 
824.9 
824.7 


740.0 
739.7 
739.5 


85.2 
85.2 
85.2 


0.5736 
0.5740 
0.5744 


1.740. 
1.734^ 
1.728^ 


0.5746.^. 
0.5767;| 
0.57882 J 


267 
268 
269 


270 


407.8533 


381.9 


1206.3 


824.4 


739.2 


85.2 


0.5748 


1.722g 


0.580920 


270 


271 
272 
273 


408.18.3.3 

408.51!^"^ 

408.84::;'^ 
00 


382.2 
382.6 
382.9 


1206.4 
1206.5 
1206.6 


824.2 
823.9 
823.7 


739.0 
73S.6 
738.4 


85.2 
85.3 
85.3 


0.5752 
0.5756 
0.5760 


1.716- 
1.709' 
1.703^ 


0.5829^. 
0.5850;} 
0.5871|J 


271 
272 
273 



SATURATED BT HAM —Continued. 



i 


II 
t 




4i 

A 


d 
.2 

i 

r 


11 

♦i 
p 


■u 

ll 

Apu 


=1 

ll 

rcdi 


6 

a 

a 
'0 
> 

1 

s 


Density. 


3 
1 1 


Ik 

7 


274 
275 
276 


409. Hon 

409.50-^5 
409.83g 


383.3 
383.6 
384.0 


1206.7 
1206.8 
1206.9 


823.4 

823.2 
822.9 


738.1 
737.9 
737.6 


85.3 
85.3 
85.3 


0.5764 
0.576S 

0.5772 


1.697. 
1.691^ 
1.6856 


0.5892^, 
0.5913;! 
0.59342^ 


274 
275 
276 


277 
278 
279 


410.48^; 
410.80^1 


384.3 
384.6 
385.0 


1207.0 
1207.1 
1207.2 


822.7 
822.5 
822.2 


737.4 
737.2 
736.9 


85.3 
85.3 
85.3 


0.5776 
0.5779 
0.5783 


1.679. 
1.673? 
1.668g 


0.5955.^-, 
0.5976^1 
0.599723 


277 
278 
279 


280 


411.1233 


385.3 


1207.3 


822.0 


736.7 


85.3 


0.5787 


1.662g 


0.602o 


280 


281 
282 
283 


411.443 

411.76'| 

412.08^1 


385.6 
386.0 
386.3 


1207.4 
1207.5 
1207.6 


821.8 
821.5 
821.3 


736.5 
736.2 
736.0 


85.3 
85.3 
85.3 


0.5791 
0.5795 
0.5799 


1.656. 
1.650^ 
1.645^ 


0.604^ 
0.606^ 
O.6O82 


281 
282 
283 


284 
285 
286 


412.4O09 
412.72^1 
413.04^1 


386.6 

387.0 
387.3 


1207.7 
1207.8 
1207.9 


821.1 
820.8 
820.6 


735.8 
735.5 
735.3 


85.3 

85.3 
85.3 


0.5803 
0.5806 
0.5810 


1.639- 
1.634'^ 
1.628^ 


0.610n 

0.612^ 
0.614^ 


284 
285 
286 


287 
288 
289 


413.36o9 
413.68^^ 
414.00g 


387.7 
388.0 
388.3 


1208.0 
1208.1 
1208.2 


820.3 
820.1 
819.9 


735.0 
734.7 
734.5 


85.3 
85.4 

85.4 


0.5814 
0.5818 
0.5822 


1.623. 
1.617^ 
1.612^ 


O.6I60 
0.618; 
O.62O2 


287 
288 
289 


290 


414.323, 


388.6 


1208.3 


819.7 


734.3 


85.4 


0.5826 


1.607g 


0.622g 


290 


291 
292 
293 


414.63.3-, 
414.94^1 
415.25^1 


389.0 
389.3 
389.6 


1208.4 
1208.5 
1208.6 


819.4 
819.2 
819.0 


734.0 
733.8 
733.6 


85.4 
85.4 
85.4 


0.5829 
0.5833 
0.5837 


1.601. 
1.596'? 
1.591^ 


0.625o 
0.627^ 
0.629| 


291 
292 
293 


294 
295 
296 


415.56o. 

415.87-^t 
416.18|1 


390.0 
390.3 
390.6 


1208.7 
1208.8 
1208.9 


818.7 
818.5 
818.3 


733.3 
733.1 
732.9 


85.4 
85.4 
85.4 


0.5840 
0.5844 
0.5848 


1.585;. 
1.580^ 
1.5755 


0.631^ 
0.6.3.3; 
0.635^ 


294 
295 
296 


297 
298 
299 


416.49Q-, 
416.80*^i 
417.11^1 


390.9 
391.3 
391.6 


1209.0 
1209.1 
1209.2 


818.1 
817.8 
817.6 


732.7 
732.4 
732.2 


85.4 

85.4 
85.4 


0.5851 
0.5855 
0.5859 


1.570. 
1.564^ 
1.559g 


0.637.-, 
0.639o 
0.641^ 


297 
298 
299 


300 


417.4230 


391.9 


1209.3 


817.4 


732.0 


85.4 


0.5863 


1.554. 


0.6442 


300 


301 
302 
303 


417.723. 

418.02^^ 
418.32^^ 


392.2 
392.5 

392.8 


1209.3 
1209.4 
1209.5 


817.1 
816.9 
816.7 


731.7 
731.5 
731.3 


85.4 
85.4 
85.4 


0.5866 
0.5870 
0.5873 


1.549. 

1.544^ 

1.539- 



0.646.. 
0.648^ 
O.65O2 


301 
302 
303 


304 
305 
306 


418.62.^ 
418.92^0 
419.22^0 


393.2 
393.5 
393.8 


1209.6 
1209.7 
1209.8 


816.4 
816.2 
816.0 


731.0 
730.8 
730.6 


85.4 
85.4 
85.4 


0.5877 
0.5880 
0.5884 


1.534- 
1.529^ 
1.524^ 


0.652.. 
0.654^ 
0.656| 


304 
305 
306 


307 
308 
309 


419.52on 

419.82^X 
420.12^g 


394.1 
394.4 
394.7 


1209.9 
1210.0 
1210.1 


815.8 
815.6 
815.4 


730.4 
730.2 
730.0 


85.4 
85.4 
85.4 


0.5888 
0.5891 
0.5895 


1.520- 
1.515'^ 
1.510§ 


0.658n 
O.66O0 
0.662^ 


307 
308 
309 


310 


420.423() 


395.0 


1210.2 


815.2 


729.8 


85.4 


0.5898 


I..50.55 


0.6642 


310 


311 
312 
313 


420.723. 
421.02^J^ 
421.32^^ 


395.4 
395.7 
396.0 


1210.3 
1210.4 
1210.4 


814.9 
814.7 
814.4 


729.5 
729.3 
729.0 


85.4 
85.4 
85.4 


0.5902 
0.5905 
0.5909 


1..500. 
1.496- 
1.49lg 


0.666^ 
0.6680 
0.671^ 


311 
312 
313 



19 



SATURATED STB AM— Continued. 



n 

p 


li 
t 


2 

1 
1 


1 


i 

4 
r 

r 


ll 
III 

p 


I2 

Apu 


-3 

(cdt 
J T 


3 

I 
1 


Density. 


t 

11 
Hi 

P 


5=1 
111. 

V 


314 
315 
316 

317 
318 
319 

320 

321 
322 
323 

324 
325 
326 

327 
328 
329 

330 

331 
332 
333 

334 
335 
336 


421.623Q 
421.92;^^ 
422.21^^ 

422.0O2Q 

422.79|^ 
423.08,^^ 

423.372P 

423.6629 
423.95^^ 
424.24g 

424.5329 
424.82^^ 
425.10^° 

42o.382„ 

425.962^ 

426.2423 

426.52oQ 
426.80^0 
427.08g 

427.36oft 
427.64^° 
427.92^^ 


396.3 
396.6 
396.9 

397.2 
397.5 
397.8 

398.1 

398.4 
398.7 
399.0 

399.3 
399.6 
399.9 

400.2 
400.5 
400.8 

401.1 

401.4 

401.7 
402.0 

402.3 
402.6 
402.9 


1210.5 
1210.6 
1210.7 

1210.8 
1210.9 
1211.0 

1211.1 

1211.2 
1211.2 
1211.3 

1211.4 
1211.5 
1211.6 

1211.7 
1211.8 
1211.9 

1211.9 

1212.0 
1212.1 
1212.2 

1212.3 
1212.4 
1212.5 


814.2 
814.0 
813.8 

813.6 
813.4 
813.2 

813.0 

812.8 
812.5 
812.3 

812.1 
811.9 
811.7 

811.5 
811.3 
811.1 

810.8 

810.6 
810.4 
810.2 

810.0 
809.8 
809.6 


728.7 
728.5 
728.3 

728.1 
727.9 

727.7 

727.5 

727.3 
727.0 
726.8 

726.6 
726.4 
726.2 

726.0 

725.8 
725.6 

725.3 

725.1 
724.9 

724.7 

724.5 
724.3 
724.1 


85.5 
85.5 
85.5 

85.5 
85.5 
85.5 

85.5 

85.5 
85.5 
85.5 

85.5 
85.5 
85.5 

85.5 
85.5 
85.5 

85.5 

85.5 
85.5 
85.5 

85.5 
85.5 
85.5 


0.5913 
0.5916 
0.5919 

0.5923 
0.5926 
0.5930 

0.5933 

0.5937 
0.5940 
0.5944 

0.5947 
0..O950 
0.5954 

0.5957 
0.5960 
0.5964 

0.5967 

0.5970 
0.5974 
0.5977 

0.5980 
0.5984 
0.5987 


1.486- 
1.481? 
1.477^ 

1.472, 
1.468^ 
1.464^ 

1.4595 

1.454. 
I.450J 
1.445^ 

1.441 1 
1.437^ 
1.432^ 

1.428, 
1.424^ 
1.420| 

1.4154 

1.407? 
1.403| 

1.399, 
1.395; 
1.39r 


0.673^ 
0.675^ 
0.677^ 

0.6790 
O.68I; 
0.683| 

0.6853 

0.688^ 
0.690o 
0.692| 

0.694n 
0.696n 
0.6982 

0.700.5 
0.702; 
0.7042 

0.7072 

0.709„ 
O.71I0 
0.713| 

0.715p 
0.7l7p 
0.719^ 


314 
315 
316 

317 
318 
319 

320 

321 
322 
323 

324 
325 
326 

327 
328 
329 

330 

331 
332 
333 

334 
335 
336 





20 



Table hi. 

SATURATED STEAM. 

FREXCH ITNITS. 



£b 



1 
2 
3 

4 
5 
6 

7 
8 
9 

10 

11 
12 
13 

14 
15 
16 

17 
18 
19 

20 

21 
22 
23 

24 
25 
26 

27 
28 
29 

30 



4.6O2339 

6. 100 ,o« 

-m^465 
^001^93 

7.494-2= 
^•^'%91 



028 



9.167 
9.795, 



10.460^5^ 

11.91Uq. 
12.702g^ 
13.539gg^ 



14.423. 
15.360, 
16.349 

17.395 

18.498 
19.663 
20.892: 



937 
989 
1046 

1103 

1165 
1229 
1296 



24.994j^|;^ 

26.510..Q. 
28.107}^^^ 
29.786}^^? 



31.553 



1858 



12 

la 


1 


■a 

1 


? 


A 


0.000 


606.5 


1.007 
2.014 
3.022 


606.8 
607.1 
607.4 


4.029 
5.036 
6.040 


607.7 
608.0 
608.3 


7.045 
8.049 
9.054 


608.6 
608.9 
609.2 


10.058 


609.6 


11.060 
12.061 
13.063 


609.9 
610.2 
610.5 


14.064 
15.066 
16.066 


610.8 
611.1 
611.4 


17.066 
18.066 
19.066 


611.7 
612.0 
612,3 


20.066 


612.6 


21.064 
22.063 
23.061 


612.9 
613.2 
613.5 


24.059 
25.058 
26.053 


613.8 
614.1 
614.4 


27.048 
28.042 
29.037 


-614.7 
615.0 
615.3 


30.032 


615.7 



t> 



606.5 

605.8 
605.1 
604.4 

603.7 
603.0 
602.3 

601.6 
600.9 
600.1 

599.5 

598.8 
598.1 
597.4 

596.7 
696.0 
595.3 

594.6 
593.9 
593.2 

692.5 

591.8 
591.1 
590.4 

689.7 
589.0 

588.3 

587.7 
587.0 
586.3 

585.7 



p 



575.5 

574.7 
573.9 
573.2 

572.4 
571.6 
570.8 

570.0 
569.3 
568.4 

567.7 

566.9 
566.1 
565.3 

564.5 
.563.8 
563.0 

562.2 
561.4 
560.6 

559.8 

559.0 
558.2 
557.5 

556.7 
555.9 
555.1 

554.4 
553.6 
552.8 

552.1 






31.0 

31.1 
31.2 
31.2 

31.3 
31.4 
31.5 

31.6 
31.6 
31.7 

31.8 

31.9 
32.0 
32.1 

32.2 
32.2 
32.3 

32.4 
32.5 
32.6 

32.7 

32.8 
32.9 
32.9 

33.0 
33.1 
33.2 

33.3 
33.4 
33.5 

33.6 



O-r; 

C45 



rcdt 
J T 



0.00000 

0.00367 
0.00733 
0.01098 

0.01461 
0.01823 
0.02183 

0.02542 
0.02899 
0.03255 

0.03609 

0.03962 
0.04313 
0.04663 

0.05012 
0.05359 
0.05705 

0.06050 
0.06330 
0.06735 

0.07076 

0.07415 
0.07754 
0.08091 

0.08427 
0.08762 
0.09094 

0.09426 
0.09756 
0.10085 

0.10413 



211.5 

197.7 
184.6 
172.4 

161.2 
150.8, 
141.2, 



138 

131 

122 
112 

104 

96 

90 



132.2, 
123.9; 

116.2: 

109.0, 
102.3 



67 



96.09 
90.19; 

84.76 

79.( 

74.97; 

70.56 
66.44 
62.58! 



62 

590 

543 

507 
472 
441 



412 



'360 



DENsmr. 






^« 



arr-i 






0.004730^ 

0.005057 
0.00541' 
0.005800; 

0.006203 
0.006630' 
O.OO7O8O; 

0.007561 
0.008069 
0.008608 



'327 

360 
383 
403 

;427 

508 
529 
569 



0.009177, 



602 



0.009779, 



0.01041 
0.01108 



631 



0.01179^^ 
0.01255i^ 
0.01334^^ 



0.01417 
0.01505', 
0.01598r 



88 



68.9833^ 0.01695jQ3 



55.6I0.. 
49.51^^^ 



46.74, 
44.15; 
41.72; 



259 
243 



227 



).45, 



37.31 
35.30 

33.42 



214 
201 
188 

177 



0.01798. 
0.01906 
0.02020 



108 
114 
119 



0.021.39. g« 

0.02265|qo 
0.02397|^g 

0.02535i45 
0.02680}JR 
0.02833|52 



0.02992 



168 



1 
2 
3 

4 
5 
6 

7 
8 
9 

10 

11 
12 
13 

14 
15 
16 

17 
18 
19 

20 

21 
22 

23 

24 
25 
26 

27 
28 
29 

30 



21 



SATURATED &1EA.M — Continued. 



1-2 









31 
32 



34 
35 
36 

37 
38 
39 

40 

41 
42 
43 



44 
45 



47 
48 
49 

50 

51 
52 
53 



57 
58 
59 

60 

61 
62 
63 

64 
65 
66 

67 
68 
69 

70 



33.411 



35.364 



19oi 



33 , 37.410 



,2052 



2155 



39.5 1 
41.{ 



|l2262 

49.308^^!, 
52.052^^^- 

54.9I3Q1 

57.92o., 

64.35^-^ 



^^ 



r., ia3o0 

46 75.16^^^ 



79.10 
83.21 
87.51 

91.98 



411 
430 
447 

'467 



96.65.00 
101.54^°^ 
106.64^1? 



54 111.95.-, 

55 117.40':?2^ 

56 123.25^^^ 



142.02^-^1 
148.80^()5 



155.85 
103.18, 
170.80, 



733 
762 
792 



178.72^00 
186.95«?^ 
195.50|g 

204.38g29 
213.60^^r 

—^••^'992 



233.09 



1030 



31.027 
32.023 
33.018 

34.014 
35.009 
36.007 

37.005 
38.004 
39.002 

40.0 

41,0 
42.0 
43.0 

44.0 
45.0 
46.0 

47.0 
48.0 
49.0 

50.0 

.51.0 
52.1 
53.1 

54.1 
55.1 
50.1 

57.1 
58.1 
50.1 

60.1 

61.1 
02.1 
63.1 

64.2 
65.2 
66.2 

67.2 

68.2 
69.2 

70.2 



616.0 
616.3 
616.6 



o 

•Si- 



585.0 
584.3 
583.6 



616.9 582.9 
617.2 582.2 
617.5 581.5 



617.8 
618.1 
018.4 



580.8 
580.1 
579.4 



618.7 I 578.7 



619.0 
619.3 
619.6 

619.9 
620.2 
620.5 

620.8 
621.1 
621.4 

621.8 

622.1 
622.4 
622.7 

623.0 
623.3 
623.6 

623.9 
624.2 
624.5 

624.8 

625.1 
625.4 
625.7 

626.0 
626.3 
626.6 

626.9 
627.2 
627.5 

627.9 



578.0 
577.3 
576.6 

575.9 
575.2 
574.5 

573.8 
573.1 
572.4 

571.8 

571.1 
570.3 
569.6 

568.9 
508.2 
567.5 

566.8 
566.1 
565.4 

564.7 

564.0 
503.3 
562.6 

561.8 
561.1 
560.4 

559.7 
559.0 
558.3 

557.7 






551.3 
550.5 
549.7 

548.9 
548.2 
547.4 

546.6 
.545.8 
545.0 

544.2 

543.4 
542.6 
641.8 

541.0 
540.2 
539.4 

538.6 
537.8 
537.0 

536.3 

535.5 
534.6 
533.8 

533.0 
532.2 
531.4 

530.7 
529.9 
529.1 

528.3 

527.5 
526.7 
525.9 

525.0 
524.2 
523.4 

522.6 

521.8 
521.0 

520.3 



Apu 



33.7 
33.8 
33.9 

34.0 
34.0 
34.1 

34.2 
34.3 
34.4 

34.5 

34.6 
34.7 
34.8 

34.9 
35.0 
35.1 

a5.2 
35.3 
35.4 

35.5 

35.6 
35.7 
35.8 

35.9 
36.0 
36.1 

36.1 

36.2 
30.3 

36.4 

36.5 
30.0 
36.7 

36.8 
36.9 
37.0 

37.1 
37.2 
37.3 

37.4 



go 
J T 



0.10740 
0.11067 
0.11392 

0.11716 
0.12039 
0.12362 

0.12683 
0.13004 
0.13324 

0.1364 

0.1396 
0.1428 
0.1459 

0.1491 
0.1522 
0.1554 

0.1585 
0.1017 
0.1048 

0.1679 

0.1710 
0.1741 
0.1772 

0.1803 
0.1833 
0.1804 

0.1895 
0.1925 
0.1956 

0.1986 

0.2016 
0.2046 
0.2076 

0.2106 
0.2136 
0.2166 

0.2196 
2225 
0.2254 

0.2284 



31.65. ^« 
28.42|56 

24.25JI 



23.02 
21.80 
20.77 

19.749, 

18.76o, 

17.84^; 
16.98g; 

16.16^, 
15.394 



116 
109 
103 



14.66 



13.97ft« 
13.31^^ 
12.69^ 



12.11 

11.56 
11.03 
10.53 



10.06 4. 
9.610]|3 
9.185]^; 



8.782 
8.309: 
8.030; 

7.687 



383 
303 
349 

325 



Density. 






0.03160.^- 
0.03335|'5 
0.03519Jg3 



0.03712, 



0.03913 
0.04124 



201 
211 
220 



0.04344.^on 
0.04574^^^ 
0.04815-^} 

0.05066233 

0.05329..-- 
0.05604^''? 
0.05889293 

0.06187o1r^ 
0.00497SiV 
0.06822^3^ 

O.O7I6O0-0 
0.07512^^ 



0.07878c 



0.08259, 

0.08653 
0.09069 
0.09497 



381 
'394 

410 

428 
443 



0.09940,-^ 
0.1041,0 '^ 
0.1089^'^ 

0.1139,0 
0.1191'^^ 
0.1245?^ 

0.1301.^ 



7.302.3,, 0.1358^^ 
7.051'^^i 0.1418^^ 
6.754|{ 0.1481^^ 



0.1546^7 
0.1613^^ 
0.1682?:/ 



6.470269 
6.201.fJ^ 
5.947|'^| 

5.705.^00 
5.472;g 

5-250^10 
5.O4O201 



0.17.^3-, 
0.1827iJ 
0.1905^Q 



0.1985 



82 



SATURATED STB AM— Continued. 






71 
72 
73 

74 
75 
76 

77 
78 
79 

80 

81 
82 
83 

84 
85 
86 

87 
88 
89 

90 

91 
92 
93 

94 
95 
96 

97 
98 
99 

100 

101 
102 
103 

104 
105 
106 

107 
108 
109 

110 






243.39 
254.07 
265.14 



1068 
1107 
1148 



276.62^jgg 

2oO.0l<f)q9 

300.83^27^ 



313.59 
326.80 
340.48 



354.63 



1321 
1368 
1415 

1464 



P-2^1514 
384.41. --,« 

400.08}^^ 



416.27 
433.01 
450.31 

468.18 
486.64 
505.71 



1674 

1730 

1787 

1846 
1907 
1969 



525.40^032 

566. < 022(34 
088.34^233 

657:45^|]g 

2S-?22524 
^S-j'2602 



(60.00 



275 



S7.5, 



815.8 
845.0; 



283 
292 
301 



875.1ooQ 
906.0oVq 
937.93^^^ 



970.7 
1004.4 
1039.1: 



337 
347 



356 
1074.73,7 



3 

o 



71.2 

72.2 
73.2 

74.2 
75.2 

76.2 

77.3 
78.3 
79.3 

80.3 

81.3 
82.3 
83.3 

84.3 
85.3 
86.3 

87.3 
88.3 
89.4 

90.4 

91.4 
92.4 
93.4 

94.4 
95.4 
96.4 

97.4 
98.4 
99.4 

100.4 

101.4 
102.5 
103.5 

104.5 
105.5 
106.5 

107.5 
108.5 
109.5 

110.5 



628.2 

628.5 
628.8 

629.1 
629.4 
629.7 

630.0 
630.3 
630.6 

630.9 

631.2 
631.5 
631.8 

632.1 
632.4 
632.7 

633.0 
633.3 
633.6 

634.0 

634.3 
634.6 
634.9 

635.2 
635.5 
635.8 

636.1 
636.4 
636.7 

637.0 

637.3 
637.6 
637.9 

638.2 
638.5 



639.1 
639.4 
639.7 

640.1 



557.0 
556.3 
555.6 

554.9 
554.2 
553.5 

552.7 
552.0 
551.3 

550.6 

549.9 
549.2 

548.5 

547.8 
547.1 
546.4 

545.7 
545.0 
544.2 

543.6 

542.9 
542.2 
541.5 

540.8 
540.1 
539.4 

538.7 
538.0 
537.3 

536.6 

535.9 
535.1 
534.4 

533.7 
533.0 
532.3 

531.6 
530.9 
530.2 

529.6 






519.5 
518.7 
517.9 

517.1 

516.3 
515.5 

514.6 
513.8 
513.0 

512.3 

511.5 
510.7 
509.9 

509.1 
508.3 
507.5 

506.7 
505.9 
505.0 

504.3 

503.6 
502.8 
502.0 

501.2 
500.4 
499.6 

498.8 
498.1 
497.3 

496.4 

495.6 
494.7 
493.9 

493.2 
492.4 
491.6 

490.8 
490,1 
489.3 

488.6 
23 



^ o 
0) op" 



37.5 
37.6 

37.7 

37.8 
37.9 
38.0 

38.1 

38.2 
38.3 

38.3 

38.4 
38.5 
38.6 

38.7 
38.8 
38.9 

39.0 
39.1 
39.2 

39.3 

39.3 
39.4 
39.5 

39.6 

39.7 
39.8 

39.9 
39.9 
40.0 

40.2 

40.3 
40.4 
40.5 

40.5 
40.6 
40.7 

40.8 
40.8 
40.9 

41.0 






rcdf 



0.2313 

0.2342 
0.2371 

0.2400 
0.2429 
0.2458 

0.2487 
0.2516 
0.2544 

0.2573 

0.2601 
0.2630 
0.2658 



0. 

0.2714 

0.2742 

0.2770 
0.2798 
0.2826 

0.2854 

0.2881 
0.2909 
0.2937 

0.2964 
0.2991 
0,3019 

0.3046 
0.3073 
0.3100 

0.3127 

0.31.54 
0.3181 
0.3208 

0.3235 
0.3261 

3288 

0.3314 
0.3341 
0.3867 

0.3393 



4.839 
4.648 
4.465 

4.291 
4.124 
3.965 

3.813 
3.668 
3.529 

3.397 

3.270 
3.149 
3.033 



191 

183 
174 

167 
159 
152 

145 
139 
132 

127 

121 
116 
111 



2.922^. 

2.616 

2.523^5 

2.433^g 

2.34782 
2. 265^0 



2A86i 

2.110^0 

<2 

2.038.0 
1.968'!; 
1-901^ 

|-S562 
1.715,-^ 



1.661 



52 



1.609... 
1.556'?'j* 
1-505^9 

1.45647 
1.409|{ 
1.365^^ 

1.320,2 

1.278^2 
1.248^0 



1.209 



37 



Density. 






0.2067^. 
0.2151°J 
0.2239yJ 



0.2330, 
0.2425 

0.2522 

0.2623 

0.2726 
0.2833 

0.2944 

0.3058 
0.3176 
0.3298: 

0.3423 
0.3552 
0.3685 

0.3822 
0.3965 
0.4111 



95 
97 
101 

103 
107 
111 

114 

118 
122 
125 

129 
133 
137 

143 

146 
149 



0.4260,55 

^•Ifi5l60 
0.4739}^^ 



0.4908 
0.5081 
0.5261 



173 

180 
184 



0.5445 



0.5636 
0.5831 

0.6024 

0.6219 
0.6427 
0.6645, 



:i91 



195 
191 

195 

208 
218 
223 



0.6868.,^p 

o.7097;o;; 

0.7333-g 

0.7576^^0 
0.7825^^^ 

0.8080|gg 



0.8340, 



268 



ic^ 



71 
72 
73 

74 
75 
76 

77 
78 
79 

80 

81 
82 
83 

84 
85 
86 

87 
88 
89 

SO 

91 
92 
93 

94 
95 
96 

97 
98 
99 

100 

101 
102 
103 

104 
105 
106 

107 
108 
109 

110 



S ATtTHATED STEAM — Continued. 



si 






111 

112 
113 

114 
115 
116 

117 
118 
119 

120 

121 
122 
123 

124 
125 
126 

127 
128 
129 

130 

131 
132 
133 

134 
135 
136 

137 
138 
139 

140 

141 
142 
143 

144 
145 
146 

147 
148 
149 

150 






'So 



1111.4 

1149 

1187.9 



377 

388 
398 



1310.7^g^ 

1353.9< ii 
1398.37^3 
1443.8^^ 



1490.5 

1538.5 
1587.7 
1638.3 



480 



492 
506 
518 



1743.3gg 
1797.8^^^ 

I853.75.3 

1911. 0'?^-^ 
1969.7'^S7 



2029.8, 

2091.5 
2154.8! 
2219.5 

2285.8, 



617 

633 
'647 
663 



679 
2423:2^^5 

2494.4... 

2567. 2!^^ 
2641.7{g 

2717.9.S0 

2961411 

3040.8q-q 
3126.152-^ 
3213.38^1 

3302. 5qi. 
3393.6^^} 
3486.7952 



3581.9, 



972 



111.5 
112.5 
113.5 

114.6 
115.6 
116.6 

117.6 
118.6 
119.6 

120.6 

121.6 
122.6 
123.6 

124.6 
125.6 
126.6 

127.7 
128.7 
129.7 

130.7 

131.7 
132.7 
133.7 

134.7 
135.7 
136.7 

137.7 

138.7 
139.8 

140.8 

141.8 
142.8 
143.8 

144.8 

14.5.8 
146.8 

147.8 
148.8 
149.8 

150.8 



640.4 
640.7 
641.0 

641.3 
641.6 
641.9 

642.2 
642.5 
642.8 

643.1 

643.4 
643.7 
644.0 

644.3 
644.6 
644.9 

645.2 
645.5 
645.8 

646.2 

046.5 
646.8 
647.1 

647.4 

647.7 
648.0 

648.3 
648.6 
648.9 

649.2 

649.5 
649.8 
650.1 

650.4 
650.7 
651.0 

651.3 
651.6 
651.9 

652.3 



O c3 

15> 



528.9 
528.2 
527.5 

526.7 
526.0 
525.3 

524.6 
523.9 
523.2 

522.5 

521.8 
521.1 
520.4 

519.7 
519.0 
518.3 

517.5 
516.8 
516.1 

515.5 

514.8 
514.1 
513.4 

512.7 
512.0 
511.3 

510.6 
509.9 
509.1 

508.4 

507.7 
507.0 
506.3 

505.6 
504.9 
504.2 

503.5 
502.8 
502.1 

501.5 



487.8 
487.0 
486.3 

485.4 
484.6 
483.8 

483.1 
482.3 
481.5 

480.7 

480.0 
479.2 
478.4 

477.6 
476.8 
476.1 

475.2 
474.4 
473.6 

473.0 

472.2 
471.4 
470.6 

469.8 
4G0.1 
468.3 

467.5 
466.7 
465.9 

465.1 

464.3 
463.5 

462.8 

462.0 
461.2 
460.4 

459.6 
458.9 
4.58.1 

457.4 



1*0^ 



41.1 
41.2 
41.2 

41.3 
41.4 
41.5 

41.5 
41.6 
41.7 

41.8 

41.8 
41.9 
42.0 

42.1 
42.2 
42.2 

42.3 
42.4 
42.5 

42.5 

42.6 

42.7 
42.8 

42.9 

42.9 
43.0 

43.1 
43.2 
43.2 

43.3 

43.4 
43.5 
43.5 

4:3.6 
43.7 
43.8 

43.9 
43.9 
44.0 

44.1 



t-. 



•rcdi 
J T 



0.3420 
0.3446 
0.3471 

0.3498 
0.3524 
0.3550 

0.3576 
0.3601 
0.3627 

0.3653 

0.3678 
0.3704 
0.3729 

0.3755 
0.3780 
0.3805 

0.3830 
0.3856 
0.3881 

0.3906 

0.3931 
0.3955 
0.3980 

0.4005 
0.4030 
0.4054 

0.4079 
0.4103 
0.4128 

0.4152 

0.4177 
0.4201 
0.4225 

0.4249 
0.4273 
0.4297 

0.4321 
0.4325 
0.4369 

0.4393 



1.162, 
1.126^ 
1.091" 



1.057 0.9 
1.025 ^f 
0.9942299 

0.9643nQo 
0.9354^r 
0.90762gg 



0.8808, 

0.8550 
0.8300: 
0.8059 



'258 



250 
241 
233 



0.7826. 




-Ano224 
.6022^(3 



0.73862 J ^ 

0.7175.,.o 
0.6973:^^ 
0.6778}^:^ 

0.6591iS3 

0.6408.^. 

0.623lJ'(^ 
0.606lJ^0 

0.5896..^ 
0.5736^0 

0.5583^^9 



0.54.34 
0.5289: 
0.5149 

0.5013 

0.4883 
0.4756 
0.4633 



Dexsitt. 



145 
140 
136 

130 

127 
123 
119 



O.4514..5 
0.4399|{'^ 
0.4287jjg 

0.4179^05 
0.4074{^'J 
0.397393 

0.3875nfi 



y 



0.8608.^^- 



0.8883 
0.9166; 



275 

283 
290 



0.9456^00 

0.9755^^^ 

1.006oJ^^ 



1.037. 
1.069; 
1.102; 



1.1353. 

I.I7O3. 
1.205';!2 
1.241^^ 

1.278ow 
1.315^A 



1.354 



I.434J? 
1.475^ 

1.517^3 

1.560,^ 
1.605^2 
1.650^^ 

1.696,^ 
1 743 

i:79i^g 



1.840 
1.891 
1.942 



1.995 



2.048~. 



2.10; 
2.158'^: 



55 



57 

2.215.^ 
2.273"! 

2-232^0 

2.392g2 
2.454^; 
2.517g 



.581 



65 



SATURATED STEAM — Continued. 



•P 



151 
152 
153 

154 
155 
156 

157 
158 
159 

160 

161 
162 
163 

164 
165 
166 

167 
168 
169 

170 

171 
172 
173 

174 
175 
176 

177 
178 
179 

180 

181 
182 
183 

184 
185 
186 

187 
188 
189 

190 






3679.1 

3778.4 
3879. 



993 
1014 
1035 



3983.3-, ^.« 
4089.0JJ^2' 



4307.1 
4419.5 
4534.3 

4651.4 



1124 
1148 
1171 

1195 



4770. 9, .-.-iQ 
4892.7^240 
5017. llf 

5^73- 129 
5405. jg^ 



5539. 
5676. 
5816. 

5959. 

6104. 
6251. 
6402. 

6555. 
6712. 
6871. 

7033. 
7198. 
7366. 

7537. 



137 
140 
143 

145 

147 
151 
153 

157 

159 
162 



7712. 

7889. 
8070. 

8253. 
8440. 
8631. 

8824. 
9021. 
9222. 

9426. 



165 
168 
171 

175 

177 
181 
183 

187 
191 
193 

197 
201 
204 

207 



151.8 
152.9 
153.9 

154.9 
155.9 
156.9 

158.0 
159.0 
160.1 

161.1 

162.2 
163.2 
164.2 

165.3 
166.3 
167.4 

168.4 
169.5 
170.5 

171.6 

172.6 
173.7 
174.7 

175.8 
176.8 

177.8 

178.9 
179.9 
181.0 

182.0 

183.1 
184.1 
185.2 

186.2 
187.3 
188.3 

189.4 
190.4 
191.4 

192.5 



652.6 
652.9 
653.2 

653.5 

653.8 
654.1 

654.4 
654.7 
655.0 

655.3 

655.6 
655.9 
656.2 

656.5 
656.8 
657.1 

657.4 

657.7 
658.0 

658.4 

658.7 
659.0 
659.3 

659.6 
659.9 
660.2 

660.5 
660.8 
661.1 

661.4 

661.7 
662.0 
662.3 

662.6 
662.9 
663.2 

663.5 
663.8 
664.1 

664.5 






500.8 
500.0 
499.3 

498.6 
497.9 
497.2 

496.4 
495.7 
494.9 

494.2 

493.4 
492.7 
492.0 

491.2 
490.5 
489.7 

489.0 

488.2 
487.5 

486.8 

486.1 
485.3 
484.6 

483.8 
483.1 
482.4 

481.6 
480.9 
480.1 

479.4 

478.6 
477.9 
477.1 

476.4 
475.6 
474.9 

474.1 
473.4 

472.7 

472.0 



'3 3 . 



456.6 
455.8 
455.0 

454.2 
453.4 
452.7 

451.8 
450.0 
449.2 

449.4 

448.5 
447.7 
447.0 

446.1 
445.3 
444.5 

443.7 
442.9 
442.1 

441.3 

440.5 

439.7 
438.9 

438.1 
437.3 
436.5 

435.7 
434.9 
434.0 

433.3 

432.4 
431.7 
430.8 

430.1 
429.2 
428.5 

427.6 
426.9 
426.1 

425.3 

25 






44.2 
44.2 
44.3 

44.4 
44.5 
44.5 

44.6 
44.7 
44.7 

44.8 

44.9 
45.0 
45.0 



45.3 
45.3 
45.4 

45.5 

45.6 
45.6 
45.7 

45.7 
45.8 
45.9 

45.9 
46.0 
46.1 

46.1 

46.2 
46.2 
46.3 

46.3 
46.4 
46.4 

46.5 
46.5 
■46.6 

46.7 



0-™ 



J T 



0.4417 
0.4440 
0.4464 

0.4488 
0.4511 
0.4536 

0.4560 
0.4584 
0.4608 

0.4633 

0.4657 
0.4681 
0.4705 



45.1 0.4729 

45.2 0.4752 
45.2 0.4776 



0.4800 
0.4824 
0.4847 

0.4871 

0.4895 
0.4918 
0.4941 

0.4965 

0.4988 
0.5011 

0.5035 
0.5058 
0.5081 

0.5104 

0.5127 
0.5150 
0.5173 

0.5196 
0.5219 
0.5242 

0.5264 
0.5287 
0.5310 

0.5332 



0.3779, 
0.3686, 
0.3596, 



0.3509q^ 
0.3424^^ 
0.3342| 

0.3262^0 
0.3184i^ 
0.3108^^ 



0.3035, 

0.2964 

0.2895' 
0.2828| 

0.2762, 



0.2699; 
0.263 



,63 
62 
*60 



0.2577,. 
0.25192^ 
0.2462'3i 

00 

0.2407.0 

0.2354.^ 
0.2302'?f 
0.225r?J 

0.2201 ,^ 
0.21537^ 
0.2106|i 

0.2061 , . 



Density. 






0.1973; 

0.1931 

0.1890 
0.1850! 
0.1811; 



41 



0.1773.3^ 

0.1736:^;! 

0.1700^'' 



0.1664.3. 
0.1630:<J 
0.15973:] 



0.1564 



32 



2.646g^ 
2.713^* 

2.78lS 



2.850„^ 
2.920i^ 
2.992^^ 

3.066^. 



3.141; 

3.217^ 

8.295. 

3.374, 
3.454^ 
3.536" 



3.620.. 
3.705^^ 
3.792Si 



3!970^? 
4.061^1 

4.154^^ 

4.248.^ 
4.345^^ 
4 444^^ 

4.543.Q. 

4.644j^Ji 

4 747^^'^ 
^•'^'105 



4.852 
4.959 
5.068 



5.178 



107 
109 
110 

113 



5.291,-,, 
5.405}!^ 

5.522{1^ 



5 640. 
5.760: 
5.882 



120 
122 
125 



6.262^28 



6.392 



133 



151 
152 
153 

154 
155 
156 

157 
158 
159 

160 

161 
162 
163 

164 
165 
166 

167 
168 
169 

170 

171 
172 
173 

174 
175 
176 

177 
178 
179 

180 

181 
182 
183 

184 
185 
186 

187 
188 
189 

190 



SATURATED STB AM— Concluded. 



191 
192 
193 

194 
195 
196 

197 
198 
199 

200 

201 
202 
203 

204 
205 
206 

207 
208 
209 

210 

211 
212 
213 

214 
215 
216 

217 
218 
219 

220 






9638..- 



9844. 
10058. 

10276. 
10498. 
10724. 



211 
214 
218 

222 

226 
229 



10953.. ^oo 
11186.^:,2 
11424.--^ 



11664. 



245 



11909.249 
12158.g.^ 
12411.|,^ 



12668. 
12930. 
13195.^ 



262 
265 



270 

13465..„4 

13739.: '5 
14018.;^^ 

14301.,s^ 

14588.QQ9 
14880.^^; 
15177.3^1 

15478.3Q^ 
15785.:^l'{ 
16096.^}! 

16411.0..1 

16732.:^-;, 

17058.O-V 
ool 

17389. 



193.5 
194.6 
195.6 

196.7 
197.7 
198.8 

199.8 
200.9 
201.9 

203.0 

204.0 

205.0 
206.1 

207.1 
208.2 
209.2 

210.3 
211.3 
212.4 

213.4 

214.5 
215.5 
216.5 

217.6 

218.6 
219.7 

220.7 
221.8 
222,8 

223.9 



664.8 
665.1 
665.4 

665.7 
666.0 
666.3 

666.6 
666.9 
667.2 

667.5 

667.8 
668.1 
668.4 

668.7 
669.0 
669.3 

669.6 
669.9 
670.2 

670.6 

670.9 
671.2 
671.5 

671.8 
672.1 
672.4 

672.7 
673.0 
673.3 

673.6 



471.3 
470.5 
469.8 

469.0 
468.3 
467.5 

466.8 
466.0 
465.3 

464.5 

463.8 
463.1 
462.3 

461.6 
460.8 
460.1 

459.3 
458.6 
457.8 

457.2 

456.4 
455.7 
455.0 

454.2 
453.5 
452.7 

452.0 
451.2 
450.5 

449.7 



« - i- 



424.6 
423.7 
423.0 

422.2 
421.4 
420.6 

419.8 
419.0 
418.2 

417.4 

416.7 
415.9 
415.1 

414.4 
413.5 
412.8 

412.0 
411.3 
410.4 

409.8 

409.0 
408.3 
407.6 

406.7 
406.0 
405.2 

404.5 
403.7 
403.0 

402.2 



_, o 
Apu 



46.7 
46.8 
46.8 

46.8 
46.9 
46.9 

47.0 
47.0 
47.1 

47.1 

47.1 

47.2 
47.2 

47.2 
47.3 
47.3 

47.3 
47.3 
47.4 

47.4 

47.4 
47.4 
47.4 

47.5 
47.5 
47.5 

47.5 
47.5 
47.5 

47.5 



c^ 



f cdt 
J T 



0.5355 
0.5377 
0.5400 

0.5422 
0.5444 
0.5467 

0.5489 
5511 
0.5533 

0.5555 

0.5577 

0.5599 
0.5621 

0.5643 
0.5665 
0.5687 

0.5709 
0.5731 
0.5752 

0.5774 

0,5795 
0.5817 
0.5839 

0.5860 
0.5881 
0.5903 

0.5924 
0.5945 
0.5967 

0.5988 



0.1532.- 
0.1501!: 



0.147i: 

0.1441 
0.1412 
0.1384^ 



27 

0.1357.^^ 
0.1330^1 
0.1303^^ 



0.1277 

0.1252, 

0.1228; 
0.1204; 



25 



0.1181^.0 
0.1158^0 
0.1135^2 

0.1113.^-, 

0.1092;! 

0.1071^1 



0.1050, 

0.1030 
0.1011 
0.0992 

0.0973 
0.0954 
0.0936 

0.0918 
0.0901 
0.0884 

0.0868 



17 



16 



Dexsity. 






6.525. Oft 
6.66lf'g 
6.798^2 

6.938.,^ 
7.080J^2 

7 2-^5 "^^ 
7.52l}|5' 

7.827,5^ 

7.984j-o 
8.143}^^ 
8.305j^r 

8.470j.o 
8.639}?V 

s.sioji^ 

8.984. „ft 

9.160j!5 
9.338}^^ 

9.519^35 



9.704 
9.894 



lo.oa 

10.28, 
10.48; 
10.68; 

10.89, 
11.10 
11.31 



190 
186 



20 



£0 



11.53 






191 
192 
193 

194 
195 
196 

197 
198 
199 

200 

201 
202 
203 

204 
205 
206 

207 
208 
209 

210 

211 
212 
213 

214 
215 
216 

217 
218 
219 

220 



TABLE IV. 



SATURATED VAPOR OF ETHER. 



■d 


£b 


3 
'3 




.2 


3_ 

A 2 


ll 


2 

*3 


i 


Density. 


£-1 


<3t^ O 






a.S" 






> s 


> j^ 


«»-i cfi 


"o 


CO--- 


3 ^ 


III 


Eli 


5J 
o 


1 






fll 




!> 


tfi 


III 


1=1 






1 


|> 


1°^ 






1 




Pl 


/ 


P 


9 


A 


r 


P 


Apu 


J r 


- 


V 


t 





184.39 


0.00 


94.00 


94.00 


86.45 


7.55 


0.0000 


1.278 


0.782 





10 


286.83 


5.32 


98.44 


93.12 


85.37 


7.75 


0.01909 


0.8440 


1.185 


10 


20 


432.78 


10.70 


102.78 


92.08 


84.13 


7.95 


0.03n2 


0.5741 


1.742 


20 


30 


634.80 


16.14 


107.00 


90.86 


82.72 


8,14 


0.05593 


0.4013 


2.492 


30 


40 


907.04 


21.63 


111.11 


89.48 


81.15 


8.33 


0,07374 


0.2877 


3.746 


40 


50 


1264.8 


27.19 


115.11 


87.92 


79.41 


8.51 


0.09117 


0.2108 


4.744 


50 


60 


1725.0 


32.80 


119.00 


86.20 


77.53 


8.67 


0.1083 


0.1580 


6.329 


60 


70 


2304.9 


38.48 


122.78 


84.30 


75.49 


8.81 


0,1250 


0.1203 


8.313 


70 


80 


3022.8 


44.21 


126.44 


82.23 


73.32 


8.91 


0.1415 


0.0932 


10.73 


80 


90 


3898.3 


50.00 


130.00 


80.00 


71.03 


8,97 


0.1576 


0.0731 


13.68 


90 


100 


4953.3 


55.86 


133.44 


77.58 


68.62 


8.96 


0.1735 


0.a577 


17.33 


100 


110 


6214.6 


61.77 


136.78 


75.01 


66.13 


8.88 


0.1891 


0.0459 


21.79 


110 


120 


7719.2 


67.74 


140.00 


72.26 


03.57 


8.69 


0.2045 


0.0364 


27.47 


120 



27 



f 



Table y. 



SATURATED VAPOR OF ALCOHOL. 

FRENCH UNITS. 



1 

t 


1^ 


3 

1 


1 

I 


.1 

r 

r 


1- 
p 




J T 


6 
S 

> 

1 


Dexsitt. 


='5 

11=! 
ill 

t 


liSl 

V 





12.70 


0.00 


236.5 


236.50 


223.38 


13.12 


0.0000 


32.21 


0.03105 





10 
20 
30 


24.23 
44.46 
78.52 


5.59 
11.42 
17.49 


244.4 
252.0 
258.0 


238.81 
240.58 
240.51 


225.29 
226. .56 
226.03 


13.52 
14.02 
14.48 


0.01996 
0.04003 
0.06029 


17.39 
9.847 
5.753 


0.05750 

0.1016 

0.1738 


10 
20 
30 


40 
50 
60 


1.3.3.69 
219.90 
350.21 


23.71 
30.21 
37.37 


262.0 
264.0 
265.0 


2.38.29 
233.79 
227.63 


223.44 
218.59 
212.38 


14.85 
15.10 
15.25 


0.08073 

0.1014 

0.1223 


3.465 
2.143 
1.359 


0.2886 
0.4666 
0.7358 


40 
50 
60 


70 
80 
90 


541.15 
812.91 
1189.3 


44.58 
52.11 
59.97 


26.5.2 
265.2 
266.0 


220.62 
213.09 
206.03 


205.28 
197.69 
190.54 


15.34 
15.40 
15.49 


0.14.35 
0.1650 
0.1868 


0.88.55 
0.5921 
0.4073 


1.129 

1.689 
2.4.55 


70 
80 
90 


100 
110 
120 


1697.6 
2367.6 
3231.7 


68.18 
76.74 
85.67 


267.3 
269.6 
272.5 


199.12 

192.86 
186.83 


183.54 
177.15 
170.97 


15.58 
15.71 
15.86 


0.2090 
0.2315 
0.2544 


0.2874 
0.2083 
0.1544 


3.479 
4.801 
6.477 


100 
110 
120 


130 
140 
150 


4323.0 
5674.6 
7318.4 


94.98 
104.70 
114.82 


276.0 
280.5 
285.3 


181.02 
175.80 
170.48 


164.99 
159.55 
154.03 


16.03 
16.25 
16.45 


0.2776 
0.3013 
0.3254 


0.1170 
0.0905 
0.0714 


8.547 
11.05 
14.01 


130 
140 
150 



28 



I 



Table VI. 



SATURATED VAPOR OF CHLOROFORM. 



FRENCH UNITS. 



a 

Is. 
S « 

ill 


III 




1 

a 


c 



s 

11 


II 

•53 _ 


3 
'5 


> 

m 


Density. 






/ 


/ 


f 


A 


r 


p 


Apu 


J T 


s 


V 


t 





59.72 


0.00 


67.00 


67.00 


62.45 


4.55 


0.00000 


2.377 


0.4207 





10 
20 
30 


100.47 
160.47 
247.51 


2.33 

4.67 
7.02 


68.38 
69.75 
71.12 


66.04 
65.08 
64.10 


61.29 
60.14 
59.00 


4.75 
4.94 
5.10 


0.00836 
0.01646 
0.02432 


1.475 

0.9601 

0.6437 


0.6780 

1.042 

1.554 


10 
20 
30 


40 
50 
60 


369.26 
535.05 
755.44 


9.37 
11.74 
14.12 


72.50 
73.87 
75.25 


63.13 
62,13 
61.13 


57.87 
56.73 
55.60 


5.26 
5.40 
5.53 


0.03196 
0.03940 
0.04664 


0.4449 
0.31.55 

0.2291 


2.248 
.3.170 
4.356 


40 
50 
60 


70 
80 
90 


1042.1 
1407.6 

1865.2 


16.51 
18.91 
21.32 


76.62 
78.00 
79.37 


60.11 

59.09 
58.05 


54.45 
53.31 
52.16 


5.66 

5.78 
5.89 


0.05369 

0.06057 
0.06729 


0.1700 
0.1286 
0.0991 


5.88 

7.78 

10.09 


70 
80 
90 


100 
110 
120 


2428.5 
3111.0 
3925.7 


23.74 
26.17 
28.61 


80.75 
82.12 
83.50 


57.01 
55.95 

54.89 


51.01 

49.84 
48.67 


6.00 
6.11 
6.22 


0.07386 
0.08027 
0.08655 


0.0777 
0.0618 
0.0500 


12.87 
16.18 
20.00 


100 
110 
120 


130 
140 
150 


4885.1 
6000.2 
7280.6 


31.06 
33.52 
35.99 


84.87 
86.25 
87.62 


53.81 
.52.73 
51.63 


47.48 
46.30 
45.10 


6..33 
6.43 
6.53 


0.09270 
0.09872 
0.10462 


0.0410 
0.0340 
0.0286 


24.39 

29.4 

35.0 


130 
140 
150 


160 


8734.2 


38.47 


89.00 


50.53 


43.90 


6.63 


0.11041 


0,0243 


41.2 


160 



Table vii. 

SATURATED VAPOR OF CARBON BISULPHIDE. 

FRENCH UNITS. 



-2 

m 

t 


CD >, 

S 5 
ill 

P 


•3 
'I 

o 

1 


"3 


.2 
1 


.Si — 
^^ o 

p 


h 

^" 3 
Apu 


ll 

[cdt 
J T 


6 
£ 

> 
1 


Density. 


li 
111 

t 


.5=1 

7 





127.91 


0.00 


90.00 


90.00 


82.76 


7.24 


0.00000 


1.766 


0.5662 





10 
20 
30 


198.46 
298.03 
434.62 


2.36 
4.74 
7.13 


91.42 
92.76 
94.01 


89.06 
88.02 

86.88 


81.58 
80.31 

78.97 


7.48 
7.71 
7.91 


0.00847 
0.01670 
0.02472 


1.177 

0.8071 

0.5684 


0.8496 

1.239 

1.759 


10 
20 
30 


40 
50 
60 


617.53 
857.07 
1164.5 


9.54 
11.96 
14.41 


95.18 
96.27 
97.28 


85.64 
84.31 
82.87 


77..54 
76.04 
74.45 


8.10 
8.27 
8.42 


0.03252 
0.04013 
0.04756 


0.4098 
0.3017 
0.2264 


2.440 
3.315 
4.417 


40 
50 
60 


70 
80 
90 


1552.1 
2032.5 
2619.1 


16.86 
19.34 
21.83 


98.20 
99.04 
99.80 


81.34 
79.70 
77.97 


72.78 
71.03 
69.20 


8.56 
8.67 

8.77 


0.05482 
0.06192 
0.06886 


0.1726 
0.1338 
0.1052 


5.794 
7.473 
9.51 


70 
80 
90 


100 
110 
120 


3325.2 
4164.1 

5148.8 


24.34 

26.86 
29.40 


100.48 
101.07 
101.58 


76.14 
74.21 

72.18 


67.29 
65.31 
63.24 


8.85 
8.90 
8.94 


0.07566 
0.08233 
0.08886 


0.0837 
0.0674 
0.0549 


11.95 

14.84 
18.21 


100 
110 
120 


130 
140 
150 


6291.6 
7604.0 
9095.9 


31.96 
34.53 
37.12 


102.01 
102.36 
102.62 


70.05 
67.83 
65.50 


61.09 
58.88 
56.58 


8.96 
8.95 
8.92 


0.09527 
0.10157 
0.10775 


0.0452 
0.0375 
0.0314 


22.12 

26.7 

.31.8 


130 
140 
150 



\ 



30 



TABLE VIII. 



SATURATED VAPOR OF CARBON TETRACHLORIDE. 

TRENCH TJNITS. 



•i 


. 


12 




S3 


1 


O-M 


3 


1 


Density. 


•i 


£^ 


S j^ 


^ c 




a 


"5 "a 


■^g 




3 


<4h o 


is 




S 5 


2-i. 




N 




> g 


q-l S* 


"o 


-. O-'- 


3^ 




oil 


5^ 


:3 


•s 


"5 3 . 


= 3^ 


12 


> 


J3 


Is . 


lli 


S c » 


1 


i 


i» 


^ o 


St 


"S 

1=1 


1 
CQ 




l|l 


t 


P 


? 


A 


r 


p 


A^u 


rcdi 
J T 


^ 


V 


i 





32.95 


0.00 


52.00 


52.00 


48.54 


3.46 


0.00000 


3.272 


0.3056 


c 


10 


55.97 


1.99 


53.44 


51.45 


47.85 


3.60 


0.00714 


2.005 


0.4987 


10 


20 


90.99 


3.99 


54.86 


50.87 


47.13 


3.74 1 0.01409 


1.283 


0.7794 


20 


30 


142.27 


6.02 


56.23 


50.21 


46.33 


3.88 


0.02087 


0.8510 


1.175 


30 


40 


214.81 


8.06 


57.58 


49.52 


45.51 


4.01 


0.02749 


0.5831 


1.715 


40 


50 


314.38 


10.12 


58.88 


48.76 


44.62 


4.14 


0.03396 


0.4109 


2.4:34 


50 


60 


447.43 


12.20 


60.16 


47.96 


43.69 


4.25 


0.04028 


0.2969 


3.36S 


60 


70 


621.15 


14.30 


61.40 


47.10 


42.75 


4.35 


0.04648 


0.2192 


4.562 


70 


80 


843.29 


16.42 


62.60 


46.18 


41.74 


4.44 


0.04255 


0.1650 


6.061 


80 


90 


1122.3 


18.55 


63.77 


45.22 


40.50 


4.72 


0.05849 


0.1263 


7.92 


90 


100 


1467.1 


20.70 


64.90 


44.20 


39.62 


4.58 


0.06433 


0.0980 


10.20 


100 


110 


1887.4 


22.87 


66.01 


43.14 


38.52 


4.62 


0.07006 


0.0770 


12.99 


110 


120 


2393.7 


25.06 


67.07 


42.01 


37.36 


4.65 


0.07569 


0.0611 


16.37 


120 


130 


2996.9 


27.27 


68.10 


40.83 


36.18 


4.65 


0.08122 


0.0490 


20.41. 


130 


140 


3709.0 


29.49 


69.10 


39.61 


34.95 


4.63 


0.08666 


0.0395 


25.3 


140 


150 


4543.1 


31.73 


70.07 


38.34 


33.75 


4.59 


0.09201 


0.0321 


31.2 


150 


160 


5513.1 


34.00 


71.00 


37.00 


32.47 


4.53 


0.09729 


0.0262 


38.2 


160 



31 



Table IX. 



SATURATED VAPOR OF ACETON. 



FRENCH UNITS. 



l5 
t 




'3 

iS 

o 

1 

9 


A 


1 
1 

o a 
r 


3 

II. 

p 


Apu 


2 
"5 

r 

c 
(cdt 


S 

I 

o 
•3 

1 


Density. 


i6 
IP. 

m 
t 


■Sc| 
y 





63.33 


0.00 


140.50 


140.50 


131.82 


8.68 


0.00000 


4.275 


0.2339 





10 
20 
30 


110.32 
180.08 
280.05 


5.10 
10.29 
15.55 


144.11 
147.62 
151.03 


139.01 
137.33 
135.48 


129.51 
127.10 
124.83 


9.50 
10.17 
10.65 


0.01832 
0.03627 
0.05389 


2.686 
1.758 
1.187 


0.3723 
0.5688 
0.8425 


10 
20 
30 


40 
50 
60 


419.35 
608.81 
860.96 


20.89 
26.31 
31.81 


154.33 
157.53 
160.63 


133.44 
131.22 

128.82 


121.39 
119.86 
117.22 


11.05 
11.36 
11.60 


0.07119 

0.08820 
0.1049 


0.8227 
0.5830 
0.4215 


1.215 
1.715 

2.372 


40 
50 
60 


70 
80 
90 


1189.9 
1611.1 
2140.8 


37.39 
43.05 
48.79 


163.62 
166.51 
169.30 


126.23 
123.46 
120.51 


114.43 
111.49 
108.41 


11.80 
11.97 
12.10 


0.1214 
0.1376 
0.1536 


0.3106 
0.2.328 
0.1773 


3.220 
4.296 
5.640 


70 
80 
90 


100 
110 
120 


2796.2 
3594.3 
4552.0 


54.61 
60,50 
66.48 


171.98 
174.56 
177.04 


117.37 
114.06 
110.56 


105.17 

101.78 
98.23 


12.20 

12.28 
12.33 


0.1694 
0.1850 
0.2004 


0.1372 
0.1076 
0.0856 


7.289 
9.294 
11.68 


100 
110 
120 


130 
140 


5684.9 
7007.6 


72.54 

78.67 


179.42 
181.69 


106.88 
103.02 


94.53 
90.67 


12.35 
12.35 


0.2156 
0.2306 


0.0689 
0.0561 


14.51 
17.83 


130 
140 



I 



32 



TABLE X. 



SATURATED VAPOR OF SULPHUR DIOXIDE. 

TKENCH UNITS. 







3 

IS 

1 




1 
=1 

r 


1 = 

P « . 


4.3 
P 

11 


s 

I 

o 

1 


Density. 




.e'S| 

ti5| 


t 


p 


9 


A 


r 


p 


Apu 


s 


V 


t 


-30 


3.91 


-10.9 


87.5 


98.3 


90.87 


7.6 


0.823 


1.22 


-30 


-25 


5.08 


- 9.1 


88.1 


97.2 


89.51 


7.7 


0.642 


1.56 


-25 


-20 


6.51 


- 7.3 


88.8 


96.1 


88.35 


7.8 


0.508 


1.97 


-20 


-15 


8.27 


- 5.4 


89.5 


94.9 


87.0 


7.9 


0.407 


2.46 


-15 


-10 


10.37 


- 3.6 


90.1 


93.7 


85.7 


8.0 


0.329 


3.04 


-10 


- 5 


12.87 


- 1.8 


90.8 


92.6 


84.4 


8.1 


0.269 


3.72 


- 5 





15.84 


0.0 


91.4 


91.4 


83.2 


8.2 


0.221 


4.52 





5 


19.32 


1.8 


92.0 


90.2 


81.9 


8.3 


0.184 


5.45 


5 


10 


23.38 


3.6 


92.4 


89.0 


80.6 


8.4 


0.154 


6.51 


10 


15 


28.07 


5.5 


93.3 


87.8 


79.3 


8.5 


0.129 


7.74 


15 


20 


33.47 


7.3 


93.9 


86.6 


78.0 


8.6 


0.110 


9.13 


20 


25 


39.65 


9.1 


94.5 


85.4 


76.7 


8.7 


0.0933 


10.7 


25 


30 


46.67 


10.9 


95.1 


84.2 


75.4 


8.7 


0.0800 


12.5 


30 


35 


54.59 


12.8 


95.5 


82.9 


74.1 


8.8 


0.0689 


14.5 


35 


40 


63.50 


14.6 


96.3 


81.7 


72.8 


8.8 


0.0597 


16.8 


40 



83 



Table xi. 



SATURATED VAPOR OF AMMONIA. 

FRENCH UNITS. 



1^1 


15^ 


2 

1 


1 

o 


c 

?! 


c 

IP 


Hi 


s 

> 

1 

02 


Density. 


III 


.s'si 


t 


P 


? 


A 


r 


P 


Apu 


i 


V 


t 


-40 
-35 
-30 


7.19 

9.30 

11.92 


-37.3 
-33.0 

-28.5 


298.0 
300.0 
302.0 


335.2 
332.9 
330.5 


308.7 
305.9 
303.0 


26.5 
27.0 
27.4 


1.56 
1.23 

0.978 


0.639 
0.812 
1.02 


-40 
-35 
-30 


-25 
-20 
-15 


15.12 
19.00 
23.67 


-23.0 
-19.4 
-14.7 


303.9 
305.9 
307.9 


327.0 
325.3 
322.5 


300.0 
296.9 
293.7 


27.9 
28.9 
28.8 


0.784 
0.634 
0.518 


1.28 
1.58 
1.93 


-25 
-20 
-15 


-10 

- 5 




29.23 
35.80 
43.480, 


- 9.9 

- 5.0 
0.0 


309.8 
311.7 
313.6 


319.7 
316.7 
313.6 


290.4 
287.0 

283.5 


29.3 
29.7 
30.2 


0.426 
0.352 
0.295 


2.35 
2.84 
3.39 


-10 

- 5 




5 
10 
15 


52.41 
62.71 

74.50 


5.1 
10.2 
15.5 


315.5 
317.4 
319.3 


310.5 
307.2 
303.8 


279.9 
276.1 

272.3 


30.6 
31.0 
31.5 


0.249 
0.211 
0.180 


4.02 
4.74 
5.54 


5 
10 
15 


20 
25 
30 


87.93 
103.07 
120.08 


20.8 
26.3 
31.8 


321.1 
323.0 
324.8 


300.3 
296.7 
293.0 


268.4 
264.4 
269.2 


31.9 
32.3 

32.8 


0.155 
0.134 
0.117 


6.45 
7.45 
8.55 


20 
25 
30 


35 
40 


139.05 
160.11 


37.4 
43.2 


326.6 

328.4 


289.2 
285.2 


256.0 
251.6 


33.2 
33.6 


0.102 
0.090 


9.77 
11.07 


35 
40 






34 



TABLE XII. 



SPECIFIC GRAVITY AND SPECIFIC VOLUME OF LIQUIDS. 



Xame of Liquid. 



Alcohol, CaHgO . . . . 
Ether, C4H10O . . . . 

Chloroform 

Carbon bisulphide, CS^ 
Carbon tetrachloride, CCI4 
Aceton, CaHeO . . . . 
Sulphur Dioxide SO2 . . 
Ammonia NHq . . . . 



Specific Volume. 
Specific Gravity, compared with Water at i° C. Cubic Meters 

per Kilo. 



0.80625 

0.736 

1.527 

1.2922 

1.6320 

0.81 

1.4336 

0.6364 



Mendelejeff, 1869] 
Kopp, 1860] . 
[Thorpe, 1880] . 
Thorpe, 1880] . 
Thorpe, 1880] . 
'Zander, 1882] . 
Andreeff, 1859] 
Andreeff, 1859] 



0.001240 

0.001358 

0.000655 

0.000774 

0.000613 

0.00123 

0.0006981 

0.001571 



TABLE "S:iII. 



VOLUME OP WATER. 

Yol. at 4° 0=1. 
[Kossetti, 1871] and [Him, 1867.] 



Tempera- 
ture. 


Volume. 


Tempera- 
ture. 


Volume. 


Tempera- 
ture. 


Volume. 


Tempera- 
ture. 


Volume. 


10 


1.000253 


1 60 


1.01691 


110 


1 

1.0512 


160 


1.1018 


20 


1.001744 


70 


1.022.56 


120 


1.0599 


170 


1.1139 


30 


1.00425 


80 


1.02887 


130 


1.0694 


180 


1.1268 


40 


1.00770 


90 


1.03567 


140 


1.0795 


190 


1.1403 


50 


1.01195 


100 


1.04312 


150 


1.0903 


200 


1.1544 



35 



I 



1 






I 




fi'-^xmm, 



